CN209631151U - A kind of cyclone fluidized bed WDG pesticide granulator - Google Patents
A kind of cyclone fluidized bed WDG pesticide granulator Download PDFInfo
- Publication number
- CN209631151U CN209631151U CN201920272491.3U CN201920272491U CN209631151U CN 209631151 U CN209631151 U CN 209631151U CN 201920272491 U CN201920272491 U CN 201920272491U CN 209631151 U CN209631151 U CN 209631151U
- Authority
- CN
- China
- Prior art keywords
- agitator disk
- autoclave body
- cavity
- cloth bag
- spiral board
- 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
- 239000000575 pesticide Substances 0.000 title claims abstract description 13
- 238000005469 granulation Methods 0.000 claims abstract description 28
- 230000003179 granulation Effects 0.000 claims abstract description 28
- 239000004744 fabric Substances 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 14
- 239000007921 spray Substances 0.000 claims abstract description 14
- 238000001914 filtration Methods 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 238000003756 stirring Methods 0.000 claims description 12
- 239000003795 chemical substances by application Substances 0.000 abstract description 6
- 239000011230 binding agent Substances 0.000 description 5
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000012257 stirred material Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000005453 pelletization Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Agricultural Chemicals And Associated Chemicals (AREA)
Abstract
The utility model relates to facility for granulating technical fields, more particularly, to a kind of cyclone fluidized bed WDG pesticide granulator, including autoclave body, agitator disk, granulation spray gun, deashing cloth bag, secondary ash collector, air supply device and filtering and heating case, cavity body is provided in the autoclave body, the deashing cloth bag is arranged in cavity body, cavity body is separated into upper cavity and lower chamber spaced apart from each other by the deashing cloth bag, spiral board is provided in the lower chamber, the agitator disk is rotatably arranged on spiral board, the driving device for driving agitator disk to rotate is provided on the autoclave body, the agitator disk is located at spiral board close to one end of deashing cloth bag, a kind of cyclone fluidized bed WDG pesticide granulator of the utility model is when in use, autoclave body upper end motor driven is changed to autoclave body lower end driving agitator disk, material is all covered on agitator disk in this way, It is not in the phenomenon being ejected on agitator disk when granulation lance ejection granulation agent.
Description
Technical field
The utility model relates to facility for granulating technical fields, more particularly, to a kind of cyclone fluidized bed WDG pesticide granulator.
Background technique
Existing fluidized granulation equipment is usually arranged motor in autoclave body upper end and agitator disk is driven to be stirred material, and
It is provided with granulation spray gun in autoclave body, injection granulation agent is carried out to material, such granulation binder will be ejected into stirring disk drive shaft
On, so that having bonded material on stirring disk drive shaft, it will also make a large amount of materials from bonding and be packed together, influence to produce
The production of product.
Utility model content
Technical problem to be solved by the utility model is: being usually in autoclave body upper end to solve existing fluidized granulation equipment
Setting motor simultaneously drives agitator disk to be stirred material, and is provided with granulation spray gun in autoclave body and spray pelletizing to material and glue
Agent is tied, such granulation binder will be ejected on stirring shaft, so that having bonded material on stirring shaft, also
Meeting now provides a kind of cyclone fluidized bed WDG so that a large amount of materials from bonding and the problem of be packed together, influence the production of product
Pesticide granulator.
The technical scheme adopted by the utility model to solve the technical problem is as follows: a kind of cyclone fluidized bed WDG pesticide granulation
Machine, including autoclave body, agitator disk, granulation spray gun, deashing cloth bag, secondary ash collector, air supply device and filtering and heating case, the autoclave body
It is inside provided with cavity body, the deashing cloth bag is arranged in cavity body, and cavity body is separated by the deashing cloth bag to be spaced from each other
Upper cavity and lower chamber, be provided with spiral board in the lower chamber, the agitator disk is rotatably arranged on spiral board, the kettle
The driving device for driving agitator disk to rotate is provided on body, the agitator disk is located at spiral board close to the one of deashing cloth bag
End, the granulation spray gun are arranged in lower chamber and are located above agitator disk, and the filtering and heating case passes through external pipeline and kettle
The lower chamber of body is connected to and the one end far from agitator disk that is located at spiral board, and the autoclave body, which is located at spiral board, offers discharge port,
The input terminal of the air supply device is connected to the upper cavity of the output end of secondary ash collector and autoclave body respectively by external pipeline, institute
The input terminal for stating secondary ash collector is connected to by external pipeline with the upper cavity of autoclave body, between the secondary ash collector and autoclave body
It is provided with the first valve on external pipeline, the second valve is provided on the external pipeline between the air supply device and autoclave body.
Autoclave body upper end motor driven is changed to autoclave body lower end driving agitator disk by the utility model, and such material, which is all covered on, to be stirred
Mix on disk, be not in when pelletizing lance ejection granulation binder be ejected into stirring disk drive shaft on phenomenon, also it is avoided that
On stirring disk drive shaft the phenomenon that sizing.
Windrow on side plate in autoclave body upper plenum body in order to prevent, further, the agitator disk is close to cavity body interior plate
Place is provided with scraper plate.By the way that scraper plate is arranged close to autoclave body interior plate side in agitator disk, so that windrow is stripped off, it is not in heap
Expect phenomenon.
Further, pulser is provided on the deashing cloth bag.
The beneficial effects of the utility model are: a kind of cyclone fluidized bed WDG pesticide granulator of the utility model is when in use,
Autoclave body upper end motor driven is changed to autoclave body lower end driving agitator disk, such material is all covered on agitator disk, in granulation spray gun
Be not in the phenomenon being ejected on stirring disk drive shaft when spraying granulation agent, it is usual also to avoid existing fluidized granulation equipment
Be be arranged motor and stirring rod to be driven to be stirred material in autoclave body upper end, and be provided in autoclave body granulation spray gun to material into
Row injection granulation binder, such granulation binder will be ejected on stirring disk drive shaft, so that stirring disk drive shaft
On bonded material, will also make a large amount of materials from bonding and be packed together, influence the production of product.
Detailed description of the invention
The present invention will be further described with reference to the accompanying drawings and examples.
Fig. 1 is the principles of the present invention figure
In figure: 1, autoclave body, 101, cavity body, 102, discharge port, 2, agitator disk, 3, granulation spray gun, 4, deashing cloth bag, 5, two
Grade deduster, 6, air supply device, 7, filtering and heating case, 8, spiral board, 9, driving device, the 10, first valve, the 11, second valve,
12, scraper plate, 13, pulser, 14, upper cavity, 15, lower chamber.
Specific embodiment
Presently in connection with attached drawing, the utility model is described in more detail.These attached drawings are simplified schematic diagram,
Only illustrate the basic structure of the utility model in a schematic way, therefore it only shows composition related with the utility model.
Embodiment
As shown in Figure 1, a kind of cyclone fluidized bed WDG pesticide granulator, including it is autoclave body 1, agitator disk 2, granulation spray gun 3, clear
Grey cloth bag 4, secondary ash collector 5, air supply device 6 and filtering and heating case 7 are provided with cavity body 101 in the autoclave body 1, described clear
Grey cloth bag 4 is arranged in cavity body 101, and cavity body 101 is separated into upper cavity 14 spaced apart from each other under by the deashing cloth bag 4
Cavity 15 is provided with spiral board 8 in the lower chamber 15, and the agitator disk 2 is rotatably arranged on spiral board 8, on the autoclave body 1
It is provided with the driving device 9 for driving agitator disk 2 to rotate, the agitator disk 2 is located at spiral board 8 close to the one of deashing cloth bag 4
End, the granulation spray gun 3 are arranged in lower chamber 15 and are located above agitator disk 2, and the filtering and heating case 7 passes through external pipeline
The one end of spiral board 8 far from agitator disk 2 is connected to and is located at the lower chamber 15 of autoclave body 1, and the autoclave body 1, which is located at spiral board 8, to be opened
Equipped with discharge port 102, the input terminal of the air supply device 6 by external pipeline respectively with the output end and kettle of secondary ash collector 5
The upper cavity 14 of body 1 is connected to, and the input terminal of the secondary ash collector 5 is connected to by external pipeline with the upper cavity 14 of autoclave body 1, institute
It states and is provided with the first valve 10 on the external pipeline between secondary ash collector 5 and autoclave body 1, between the air supply device 6 and autoclave body 1
External pipeline on be provided with the second valve 11.
The agitator disk 2 is provided with scraper plate 12 at 101 interior plate of cavity body.
Pulser 13 is provided on the deashing cloth bag 4.Pulser 13 prevents deashing cloth bag 4 from blocking, and makes
The phenomenon that increasing at 1 internal pressure of autoclave body.
For a kind of above-mentioned cyclone fluidized bed WDG pesticide granulator when using, starting filtering and heating case 7 first is to autoclave body 1
Lower chamber 15 is blown, while driving device 9 drives agitator disk 2 to stir, and granulation spray gun 3 carries out injection granulation agent, lower chamber
Dust is full of in 15, the wind in lower chamber 15 generates rotational flow gas under the guiding role of spiral board 8 by spiral board 8, so that
Graininess is made under the action of rotational flow gas and agitator disk 2 in material and granulation agent, is removed more than dust by deashing cloth bag 4
Dirt, the gas after dedusting reaches upper cavity 14, and is exported by one end of air supply device 6, when the gas in upper cavity 14 needs
The second valve 11 is opened when dedusting, closes the first valve 10, and the gas in upper cavity 14 is delivered to secondary ash collector 5 by autoclave body 1
Inside be dusted, then air supply device 6 be delivered to by secondary ash collector 5 and is discharged, it is required that when secondary ash collector 5 just beat
The second valve 11 is opened, it is more environmentally friendly in this way to gas dedusting again, the first valve 10 is usually being opened, and close the second valve
11, such relative energy-saving.
The above-mentioned desirable embodiment according to the utility model is enlightenment, through the above description, relevant staff
Completely various changes and amendments can be carried out in the range of without departing from this item utility model technical idea.This item is practical
Novel technical scope is not limited to the contents of the specification, it is necessary to determine that its is technical according to scope of the claims
Range.
Claims (3)
1. a kind of cyclone fluidized bed WDG pesticide granulator, it is characterised in that: including autoclave body (1), agitator disk (2), granulation spray gun
(3), deashing cloth bag (4), secondary ash collector (5), air supply device (6) and filtering and heating case (7), the autoclave body (1) is interior to be provided with
Cavity body (101), in cavity body (101), the deashing cloth bag (4) divides cavity body (101) for deashing cloth bag (4) setting
It is divided into upper cavity spaced apart from each other (14) and lower chamber (15), is provided with spiral board (8), the stirring in the lower chamber (15)
Disk (2) is rotatably arranged on spiral board (8), and the driving device for driving agitator disk (2) to rotate is provided on the autoclave body (1)
(9), the agitator disk (2) is located at the one end of spiral board (8) close to deashing cloth bag (4), and the granulation spray gun (3) is arranged in cavity of resorption
In body (15) and it is located above agitator disk (2), the filtering and heating case (7) passes through the lower chamber of external pipeline and autoclave body (1)
(15) it is connected to and is located at the one end of spiral board (8) far from agitator disk (2), the autoclave body (1), which is located to offer at spiral board (8), unloads
Material mouth (102), the input terminal of the air supply device (6) pass through the external pipeline output end and kettle with secondary ash collector (5) respectively
The upper cavity (14) of body (1) is connected to, and the input terminal of the secondary ash collector (5) passes through the upper cavity of external pipeline and autoclave body (1)
(14) it is connected to, is provided with the first valve (10) on the external pipeline between the secondary ash collector (5) and autoclave body (1), it is described to send
The second valve (11) are provided on external pipeline between wind apparatus (6) and autoclave body (1).
2. a kind of cyclone fluidized bed WDG pesticide granulator according to claim 1, it is characterised in that: the agitator disk (2)
Scraper plate (12) are provided at cavity body (101) interior plate.
3. a kind of cyclone fluidized bed WDG pesticide granulator according to claim 1 or 2, it is characterised in that: the deashing cloth
Pulser (13) are provided on bag (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920272491.3U CN209631151U (en) | 2019-03-04 | 2019-03-04 | A kind of cyclone fluidized bed WDG pesticide granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920272491.3U CN209631151U (en) | 2019-03-04 | 2019-03-04 | A kind of cyclone fluidized bed WDG pesticide granulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209631151U true CN209631151U (en) | 2019-11-15 |
Family
ID=68495220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920272491.3U Expired - Fee Related CN209631151U (en) | 2019-03-04 | 2019-03-04 | A kind of cyclone fluidized bed WDG pesticide granulator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209631151U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115090211A (en) * | 2022-06-08 | 2022-09-23 | 苏州思萃热控材料科技有限公司 | Drying and granulating integrated equipment for preparing aluminum silicon carbide composite material |
-
2019
- 2019-03-04 CN CN201920272491.3U patent/CN209631151U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115090211A (en) * | 2022-06-08 | 2022-09-23 | 苏州思萃热控材料科技有限公司 | Drying and granulating integrated equipment for preparing aluminum silicon carbide composite material |
| CN115090211B (en) * | 2022-06-08 | 2023-09-22 | 苏州思萃热控材料科技有限公司 | Integrative equipment of stoving pelletization for preparation of aluminium carborundum combined material |
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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: 20191115 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |