CN206853622U - A kind of microbial organic fertilizer pelleting system - Google Patents
A kind of microbial organic fertilizer pelleting system Download PDFInfo
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- CN206853622U CN206853622U CN201720440938.4U CN201720440938U CN206853622U CN 206853622 U CN206853622 U CN 206853622U CN 201720440938 U CN201720440938 U CN 201720440938U CN 206853622 U CN206853622 U CN 206853622U
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- conveyer belt
- drying
- organic fertilizer
- comminutor
- drying chamber
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Abstract
The utility model discloses a kind of microbial organic fertilizer pelleting system; including the first drying induction system, vibration filtering system, the second drying induction system, comminutor and water mist spray system; the first described drying induction system includes the first drying chamber and first conveyer belt; described vibration filtering system includes housing, vibrating motor and screen cloth; the second described drying induction system includes the second drying chamber and the second conveyer belt; the head blanking pipe of described first conveyer belt is located at comminutor disk top, and described water mist spray system includes water tank, water pump and jet pipe.Compared with prior art; microbial organic fertilizer pelleting system of the present utility model; pass through the improvement to former organic fertilizer apparatus and process; solves granulating raw material humidity regulation difficulty; or because the problem of excessive impurity and block influence shaping particles effect in granulating raw material be present; the balling ratio and degree of rounding of grains of comminutor are improved, improves production efficiency.
Description
Technical field
Bio-feritlizer production equipment technology is the utility model is related to, is specifically exactly a kind of biological organic fertilizer disk
Granulating system.
Background technology
It is uniform for the ease of mechanized application, fertilising, to improve fertilizer efficiency, particle generally is made by comminutor in organic fertilizer
Shape.In the prior art, fermenting raw materials system typically is used in the manufacturing process of organic fertilizer, then raw material is crushed, passed through
After crossing belt conveyor system and automatic batching system completion raw material mixing, it is delivered to comminutor and is granulated, the finished product after causing
Metering packing system is transported to by induction system, the finished product outbound after packaging.In small processing factory, mostly using disc granulation
Machine, but because the one-time investment of the complicated granulating disc of function is larger, it is high to material requirement, so mostly using simple
Granulating disc, while the simplification of technique causes iron tramp in raw material and the cleaning of other debris not in time, granulation outcome
Difference, it finally have impact on the quality and efficiency of product.
The operation principle of disc-type granulating machine is mostly：Add the overall spherical container shaping method of water balling-up disc type, directly convey raw material powder
To pan-pelletizer, and appropriate moisture content is sprayed, in 12%-14%, raw material ball enters after pan-pelletizer in disk by centrifugal force humidity,
The effect of frictional force and gravity, along parabolic motion.Due to the caking property and plasticity of material, make ball mutual in motion process
It is bonding and gradually grow up.When the inclination angle of pan-pelletizer, Pan Biangao, the timing of the parameter such as rotating speed and moisture content one, the pellet of different-grain diameter
Leave disk side because gravity is different by different disengaging angles and scroll down through.Pellet is in continuous rolling process by the water in ball
Part is constantly expelled from surface, due to the caking property of material and the natural volatilization of surface liquid film, pellet is had certain intensity,
Then as tilt disk body rotation outside the edge discharge tray of disk.
Influence of the humidity of granulating raw material for shaping particles is very big, raw material after drying chamber is handled carry out particle into
When shape is processed, cause moisture excessive often due to finished product drying is uneven, have a strong impact on balling ratio, but because of production technology cloth
Put, cause follow-up raw material can not carry out secondary drying processing, add and have bad luck cost impact efficiency, while there is biological machine fertilizer to make
For grain machine to tilt the disk installed and used, the larger powder of humidity is placed in bottom in chassis, by the rotation of disk so that
Powder conglomeration, knot grain, but due to the reason such as high humidity cooling is fast, knot grain effect is very undesirable, and also needs to follow-up baking
Equipment for drying is dried, and very big inconvenience is brought to production.In addition in the conventional preamble link of comminutor, it is usually present miscellaneous
Thing and iron tramp etc., all have a great impact for product balling ratio, it is therefore desirable to granulating system is transformed, in time adjustment
The moisture of granulating raw material is controlled, and removes the iron tramp in raw material, improves the balling ratio and degree of rounding of grains of comminutor.
The content of the invention
The purpose of this utility model is to provide a kind of microbial organic fertilizer pelleting system, passes through the liter to common equipment technique
Level transformation, more reasonably humidity, the temperature of control organic fertilizer particles balling-up, and remove impurity therein, improve comminutor
Balling ratio and production efficiency.
The technical scheme in the invention for solving the technical problem is：A kind of microbial organic fertilizer pelleting system, bag
The first drying induction system, vibration filtering system, the second drying induction system, comminutor and microbial inoculum sprinkling system are included, it is described
First drying induction system includes the first drying chamber and first conveyer belt, and the raw material of mixing enters after the drying of the first drying chamber
Filtration system is shaken, the entrance of described vibration filtering system is arranged on the outlet port of the first drying, described vibration filtering
System includes housing, vibrating motor and screen cloth, and sufficiently loose for raw material to be carried out, the material and impurity of bulk pass through screen cloth
Intercept, avoid being directly entered granulating system, the discharging opening of the vibration filtering system is arranged on the top of the first belt conveyor, warp
The bulk material for crossing screening is delivered to comminutor by first conveyer belt, and being provided with material in the middle part of the first conveyer belt counted leads
To device, the described second drying conveying device is located at the bottom of material guide device, the described second drying induction system bag
The second drying chamber and the second conveyer belt are included, the discharging opening of the second described drying chamber is located at the afterbody of the second conveyer belt, described
The head discharging opening of second conveyer belt is located at the head discharging metastomium of first conveyer belt, under the head of described first conveyer belt
Pipe material is located at the top of comminutor disk, and described comminutor bottom cavity is connected with the first drying chamber by hot air duct,
Described microbial inoculum sprinkling system includes microbial inoculum case, water pump and jet pipe, and described jet pipe is arranged at the top of the disk of comminutor.
As optimization, the head roller of the first conveyer belt counted is permanent magnetic pulley, for removing the iron tramp in raw material.
As optimization, the motor of the head roller of described first conveyer belt is variable-frequency motor, can adjust feeding
Speed.
As optimization, described jet pipe includes vertical tube and transverse tube, and the bottom of described transverse tube is provided with some nozzles.
As optimization, described nozzle diameter along the inclined direction of disk by it is high and it is low progressively reduce, for adapting to disk
Angle of inclination.
As optimization, described hot air duct is provided with flow valve and thermometer, and described flow valve is used to adjust hot blast
Air quantity, described thermometer are used for the temperature for measuring disk bottom.
The beneficial effects of the utility model：Fertilizer granulation system of the present utility model, by former organic fertilizer equipment work
The improvement of skill, solving granulating raw material humidity regulation difficulty, humidity is excessive or humidity is too small timely and effective can not adjust, or
Because the problem of excessive impurity and block influence shaping particles effect in granulating raw material be present, the balling ratio of comminutor is improved
And degree of rounding of grains, improve production efficiency.
Brief description of the drawings
Fig. 1 is structure chart of the present utility model；
Fig. 2 is the structure chart of the utility model transverse tube；
Wherein, 1 first drying chamber, 2 vibration filtering systems, 21 vibrating motors, 22 filter screens, 3 first conveyer belts, 31 materials are led
To device, the head roller of 32 first conveyer belts, 4 second drying chambers, 5 second conveyer belts, 6 comminutors, 71 microbial inoculum casees, 72 frequency conversions
Water pump, 73 water pipelines, 74 vertical tubes, 75 transverse tubes, 76 shower nozzles, 8 hot air ducts, 81 flowmeters, 82 thermometers.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, technical solutions of the utility model are carried out clear, complete
Ground describes.
A kind of microbial organic fertilizer pelleting system of the utility model, including the first drying induction system, vibration filtering system, the
Two drying induction systems, comminutor and microbial inoculum sprinkling system, the described first drying induction system include the first drying chamber 1 and the
One conveyer belt 3, mixed raw material enter vibration filtering system 2, described vibration filtering system after the drying of the first drying chamber 1
The entrance of system 2 is arranged on the outlet port of the first drying chamber 1, described vibration filtering system 2 include housing, vibrating motor 21 and
Screen cloth 22, sufficiently loose for raw material to be carried out, the material and impurity of bulk are intercepted by screen cloth, avoid being directly entered granulation
System, the effect of granulation formation is influenceed, the discharging opening of the vibration filtering system 2 is arranged on the top of the first belt conveyor 3, warp
The bulk material for crossing screening is delivered to comminutor 6 by first conveyer belt 3, and the middle part of described first conveyer belt 3 is provided with thing
Expect guider 31, the described second drying conveying device is located at the bottom of material guide device 31, and the described second drying is defeated
System is sent to include the second drying chamber 4 and the second conveyer belt 5, the discharging opening of the second described drying chamber 4 is located at the second conveyer belt 5
Afterbody, the head discharging opening of the second described conveyer belt 5 are located at the head discharging metastomium of first conveyer belt 3, and described first
The head blanking pipe of conveyer belt 3 is located at the top of the disk of comminutor 5, the described bottom cavity of comminutor 6 and the first drying chamber 1
Connected by hot air duct 8, described microbial inoculum sprinkling system includes microbial inoculum case 71, water pump 72 and jet pipe, described jet pipe arrangement
At the top of the disk of comminutor 6.
In order to preferably remove the iron tramp in raw material, the head roller of first conveyer belt 3 is permanent magnetic pulley, permanent magnetic pulley
Bottom be provided with sub-material scraper-trough conveyer, the raw material by iron removaling by sub-material scraper-trough conveyer enter comminutor 6 disk, while first conveying
Motor with 3 head roller is variable-frequency motor, can adjust feeding speed, it is ensured that the speed of granulating, if raw material
Water deficient is sprayed, if being provided with the bottom of transverse tube 75 by the jet pipe 73 of microbial inoculum sprinkling system, it is necessary to sprayed water
Dry shower nozzle 76, the nozzle diameter of shower nozzle 76 along the inclined direction of disk, by it is high and it is low progressively reduce, for adjusting the water of microbial inoculum
Amount, is easy to water to be uniformly distributed.It is simultaneously higher in moisture, can be right by hot air duct 8 when particularly bottom deposit moisture is higher
Disk bottom carries out hot-air seasoning, while flow valve 81 is provided with hot air duct 8, can adjust the air quantity of hot blast, and
Pass through the detection temperature numerical value of thermometer 82.
In embodiment, mixed raw material is dried after simple crush into the first drying chamber 1, due to raw material
Moisture gap is larger, and drying effect is difficult to control, and after being dried by the first drying chamber 1, raw material enters vibration filtering system 2,
In the presence of vibrating motor 21, raw material is by screen cloth 22, and some effects shaping bulk materials and impurity are by screen filtration, filtering
Raw material afterwards is delivered to by first conveyer belt 3 on the disk of comminutor 6, because the head roller 32 of first conveyer belt 3 is forever
Magnet drum, the iron tramp in raw material is then removed by roller 32, and is discharged by sub-material scraper-trough conveyer, and raw material carries out comminutor 6 and carried out
Granulation formation, during preliminary granulation forming effect difference, carry out technique adjustment.
It is excessively loose in raw material, when moisture is relatively low to cause forming effect difference, microbial inoculum sprinkling system is opened, variable frequency pump 72 will
Water in microbial inoculum case 71 is sprayed by jet pipe 73, and by vertical tube 74 and the shower nozzle 76 of transverse tube 75, microbial inoculum is sprayed on to the raw material of disk
On, while the output flow of variable frequency pump 72 according to the size that needs of water, can be adjusted.
In shaping because moisture is higher, during forming effect difference, microbial inoculum sprinkling system is closed, opens the stream of hot air duct 8
Valve 81 is measured, heating drying is carried out to disk bottom, and the temperature of disk bottom is measured by thermometer 82, while observes organic fertilizer
The effect of shaping particles.
The problem of if as the first drying chamber 1 or raw material, cause the drying effect deviation of raw material, moisture is higher, can not
Shaping, then by the material guide device 31 of first conveyer belt 3, because material guide device 31 is belt thing commonly used in the art
Expect conveying technology, the technical program is no longer described in detail, material is delivered into the second drying chamber 4, passes through secondary drying
The second conveyer belt 5 that the raw material of processing passes through positioned at the bottom of the second drying chamber 4 delivers to the great wheel rear portion of first conveyer belt 3, then
Conveyed by first conveyer belt 3 and be granulated in the disk of comminutor 6 again, it is ensured that the effect and efficiency of granulation.
The advantages of general principle and principal character of the present utility model and the utility model has been shown and described above.One's own profession
The technology people of industry is it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the spirit and scope of the utility model is not departed from, the utility model can also
There are various changes and modifications, these changes and improvements are both fallen within claimed the scope of the utility model.The utility model will
Protection domain is sought by appended claims and its equivalent thereof.
Claims (6)
1. a kind of microbial organic fertilizer pelleting system, including the first drying induction system, vibration filtering system, the second drying delivery system
System, comminutor and microbial inoculum sprinkling add-on system, it is characterised in that:The first described drying induction system includes the first drying chamber
（1）And first conveyer belt（3）, described vibration filtering system（2）Entrance be arranged on the first drying chamber（1）Outlet port,
Described vibration filtering system（2）Including housing, vibrating motor（21）And screen cloth（22）, the vibration filtering system（2）Go out
Material mouth is arranged on the first belt conveyor（3）Top, described first conveyer belt（3）Middle part be provided with material guide device
（31）, described second drying conveying device is located at material guide device（31）Bottom, described second drying induction system
Including the second drying chamber（4）And second conveyer belt（5）, described the second drying chamber（4）Discharging opening be located at the second conveyer belt（5）
Afterbody, the second described conveyer belt（5）Head discharging opening be located at first conveyer belt（3）Head discharging metastomium, it is described
First conveyer belt（3）Head blanking pipe be located at comminutor（6）The top of disk, described comminutor（6）Bottom cavity
With the first drying chamber（1）Pass through hot air duct（8）Connection, described microbial inoculum sprinkling system include microbial inoculum case（71）, water pump（72）
And jet pipe, described jet pipe are arranged in comminutor（6）Disk at the top of.
A kind of 2. microbial organic fertilizer pelleting system according to claim 1, it is characterised in that:Described first conveyer belt
（3）Head roller（32）For permanent magnetic pulley.
A kind of 3. microbial organic fertilizer pelleting system according to claim 1, it is characterised in that:Described first conveyer belt
（3）Head roller（32）Motor be variable-frequency motor.
A kind of 4. microbial organic fertilizer pelleting system according to claim 1, it is characterised in that:Described jet pipe includes vertical tube
（74）With transverse tube（75）, described transverse tube（75）Bottom be provided with some nozzles（76）.
A kind of 5. microbial organic fertilizer pelleting system according to claim 4, it is characterised in that:Described nozzle（76）It is straight
Footpath reduces along disk downwardly-inclined direction.
A kind of 6. microbial organic fertilizer pelleting system according to claim 1, it is characterised in that:Described hot air duct（8）
It is provided with the flow valve of adjustment hot blast air quantity（81）And thermometer（82）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720440938.4U CN206853622U (en) | 2017-04-25 | 2017-04-25 | A kind of microbial organic fertilizer pelleting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720440938.4U CN206853622U (en) | 2017-04-25 | 2017-04-25 | A kind of microbial organic fertilizer pelleting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206853622U true CN206853622U (en) | 2018-01-09 |
Family
ID=60817945
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720440938.4U Expired - Fee Related CN206853622U (en) | 2017-04-25 | 2017-04-25 | A kind of microbial organic fertilizer pelleting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206853622U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113828242A (en) * | 2021-10-22 | 2021-12-24 | 宜昌楚农农业发展有限公司 | Organic fertilizer production system and application method thereof |
| CN113828242B (en) * | 2021-10-22 | 2024-06-04 | 宜昌楚农农业发展有限公司 | Organic fertilizer production system and application method thereof |
-
2017
- 2017-04-25 CN CN201720440938.4U patent/CN206853622U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113828242A (en) * | 2021-10-22 | 2021-12-24 | 宜昌楚农农业发展有限公司 | Organic fertilizer production system and application method thereof |
| CN113828242B (en) * | 2021-10-22 | 2024-06-04 | 宜昌楚农农业发展有限公司 | Organic fertilizer production system and application method thereof |
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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: 20180109 Termination date: 20200425 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |