CN207047121U - The production system of the carbon-based compound organic and inorganic fertilizer of biology - Google Patents
The production system of the carbon-based compound organic and inorganic fertilizer of biology Download PDFInfo
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- CN207047121U CN207047121U CN201720979455.1U CN201720979455U CN207047121U CN 207047121 U CN207047121 U CN 207047121U CN 201720979455 U CN201720979455 U CN 201720979455U CN 207047121 U CN207047121 U CN 207047121U
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Abstract
The utility model discloses a kind of production system of the carbon-based compound organic and inorganic fertilizer of biology, it includes lignite supply system, inorganic component supply system, liquid material supply system and system of processing.The utility model has the advantage of, the system design science is reasonable, by material through crush, be granulated, dry, cool down and screening process after, the underproof product of its particle diameter is back in pulverizer, reduces the waste of material, and product output qualification rate is high；Lignite supply system can crush lignite, it is ensured that the carbon source in fertilizer is in liberal supply；Lignite can be crushed and activated by lignite supply system, it is ensured that reference state humic acid and part free state humic acid in lignite are converted to fulvo acid and are absorbed by crops utilization, and then improve and apply utilization rate of the ensuing crop for fertilizer nutrient.
Description
Technical field：
Field of fertilizer production is the utility model is related to, more particularly to a kind of production system of the carbon-based compound organic and inorganic fertilizer of biology
System.
Background technology：
As large agricultural country, China always payes attention to the production and administration of organic type fertilizer, and have accumulated rich experience.With
The progress of the development of agricultural production, particularly agricultural modernization, China's agricultural development highlights the innovation that to depend on science and technology and driven
It is dynamic, support Construction of Modern Agriculture is led, using raising labor productivity, resource utilization, labor productivity as main target,
Increase production and improve productivity lay equal stress on, Cultural practice is supporting etc. is used as basic demand.In this context, many fertilizer production devices and system are put greatly
It is honorable.
At present, the production system of compound organic and inorganic fertilizer only focuses on emphasizing the proportioning of nitrogen, phosphorus, potassium, and ignores carbon
Supply, cause in field soil commonly to lack carbon, due to the long-term omission of carbon, cause the nutrient imbalance of crop,
N. P. K absorption efficiency is influenceed, ultimately causes the problem of crop growing state is bad, output capacity reduces.Meanwhile existing organic-inorganic
The production system automaticity of Chemical Mixed Fertilizer is not high, relatively low to the utilization rate of material, has a strong impact on the life of compound organic and inorganic fertilizer
The production efficiency of production system.
Utility model content：
The purpose of this utility model be to provide it is a kind of it is reasonable in design, automaticity is high, reduces the biology of material waste
The production system of carbon-based compound organic and inorganic fertilizer.
The utility model is implemented by following technical scheme：The production system of the carbon-based compound organic and inorganic fertilizer of biology, it includes
Lignite supply system, inorganic component supply system, liquid material supply system and system of processing, the work of the lignite supply system
The discharging opening for changing agitator tank is connected by measuring belt with the charging aperture of the disk mixer of the system of processing, the no unit
The discharging opening of the pulverizer of supply system is divided to pass through the charging aperture of measuring belt and the disk mixer of the system of processing
Connection, the outlet of the concentration tank of the liquid material supply system pass through flowmeter and the granulating disc of the system of processing
Inlet connects.
Further, the lignite supply system includes lignite warehouse, Raymond mill, the activation agitator tank, activator storage
Tank, the discharging opening of the lignite warehouse connect with the charging aperture of the Raymond mill, the discharging opening of the Raymond mill and the activation
The charging aperture connection of agitator tank, the activator inlet communication of the discharging opening of the activator storage tank and the activation agitator tank.
Further, the inorganic component supply system includes several a great number of elements warehouses, several trace element storages
Storehouse, main conveyor belt and the pulverizer, the discharging opening of each a great number of elements warehouse are defeated by measuring belt and the master
The conveying initiating terminal of band is sent to connect, the discharging opening of each micro- warehouse passes through measuring belt and the main conveyor belt
Conveying initiating terminal connection, the conveying end of the main conveyor belt is placed in the charging aperture of the pulverizer；The liquid material
Supply system includes glutamic acid mother liquor storage tank and the concentration tank, the outlet of the glutamic acid mother liquor storage tank by pipeline with it is described
The inlet communication of concentration tank.
Further, the system of processing include the disk mixer, the granulating disc, dryer, cooler,
Two level screening machine and returning charge tank, the discharging opening of the disk mixer are connected by the charging aperture of conveyer belt and the granulating disc
Connect, the discharging opening of the granulating disc is connected by conveyer belt with the charging aperture of the dryer, the discharging of the dryer
Mouth is connected by conveyer belt with the charging aperture of the two level screening machine, the one-level sieve oversize outlet of the two level screening machine and two
The outlet of level sieve screenings is connected by conveyer belt with the charging aperture of the returning charge tank respectively, the two level sieve sieve of the two level screening machine
Upper thing outlet is connected by conveyer belt with finished product bin, and the discharging opening of the returning charge tank is supplied by conveyer belt and the inorganic component
The charging aperture of the pulverizer of system is answered to connect.
Further, the air outlet of the granulating disc is connected by pipeline with the air inlet of deduster.
The advantages of the utility model：1st, the system design science is reasonable, and automaticity is high, by material through crushing, being granulated,
After drying, cooling and screening process, the underproof product of its particle diameter is back in pulverizer, reduces the waste of material, product
Output qualification rate is high, has saved production cost；2nd, lignite supply system can crush lignite, it is ensured that the carbon source supply in fertilizer is filled
Foot；3rd, lignite can be crushed and activated by lignite supply system, it is ensured that the rotten plant of reference state humic acid and part free state in lignite
Acid is converted to fulvo acid and is absorbed by crops utilization, and then improves and apply utilization rate of the ensuing crop for fertilizer nutrient.
Brief description of the drawings：
Fig. 1 is the schematic diagram of the utility model integrated connection.
Lignite supply system 1, lignite warehouse 11, Raymond mill 12, activate agitator tank 13, activator storage tank 14, inorganic component
Supply system 2, a great number of elements warehouse 21, micro- warehouse 22, main conveyor belt 23, pulverizer 24, liquid material supply system
3, glutamic acid mother liquor storage tank 31, concentration tank 32, system of processing 4, disk mixer 41, granulating disc 42, dryer 43, cooling
Machine 44, two level screening machine 45, returning charge tank 46, deduster 47, finished product bin 5.
Embodiment：
Embodiment 1：
As shown in figure 1, the production system of the carbon-based compound organic and inorganic fertilizer of biology, it includes lignite supply system 1, without unit
Divide supply system 2, liquid material supply system 3 and system of processing 4, the discharging opening of the activation agitator tank 13 of lignite supply system 1
It is connected by measuring belt with the charging aperture of the disk mixer 41 of system of processing 4, the pulverizer 24 of inorganic component supply system 2
Discharging opening be connected by measuring belt with the charging aperture of the disk mixer 41 of system of processing 4, liquid material supply system 3
The outlet of concentration tank 32 is connected by flowmeter with the inlet of the granulating disc 42 of system of processing 4；
Lignite supply system 1 includes lignite warehouse 11, Raymond mill 12, activation agitator tank 13, activator storage tank 14, lignite storage
The discharging opening in storehouse 11 connects with the charging aperture of Raymond mill 12, and the charging aperture of the discharging opening and activation agitator tank 13 of Raymond mill 12 connects
It is logical, the activator inlet communication of the discharging opening and activation agitator tank 13 of activator storage tank 14；
Inorganic component supply system 2 includes several a great number of elements warehouses 21, several micro- warehouse 22, main conveyings
Band 23 and pulverizer 24, the quantity of a great number of elements warehouse 21 is five in the present embodiment, and the quantity of micro- warehouse 22 is four
It is individual；The discharging opening of each a great number of elements warehouse 21 is connected by measuring belt with the conveying initiating terminal of main conveyor belt 23, each
The discharging opening of micro- warehouse 22 is connected by measuring belt with the conveying initiating terminal of main conveyor belt 23, main conveyor belt 23
Conveying end is placed in the charging aperture of pulverizer 24；
Liquid material supply system 3 includes glutamic acid mother liquor storage tank 31 and concentration tank 32, and glutamic acid mother liquor storage tank 31 goes out
Mouth passes through the inlet communication of pipeline and concentration tank 32；
System of processing 4 includes disk mixer 41, granulating disc 42, dryer 43, cooler 44, two level screening machine 45
With returning charge tank 46, the discharging opening of disk mixer 41 is connected by conveyer belt with the charging aperture of granulating disc 42, disc granulation
The discharging opening of machine 42 is connected by conveyer belt with the charging aperture of dryer 43, and the air outlet of granulating disc 42 is by pipeline with removing
The air inlet connection of dirt device 47, the discarded middle dust-filtering that deduster 47 can exclude granulating disc 42, avoids dust emission
Pollute environment；The discharging opening of dryer 43 is connected by conveyer belt with the charging aperture of two level screening machine 45, two level screening machine 45
One-level sieve oversize outlet and the outlet of two level sieve screenings are connected by conveyer belt with the charging aperture of returning charge tank 46 respectively, two level sieve
The two level sieve oversize outlet of extension set 45 is connected by conveyer belt with finished product bin 5, and the discharging opening of returning charge tank 46 passes through conveyer belt
It is connected with the charging aperture of the pulverizer 24 of inorganic component supply system 2.
The course of work：
Lignite is entered in Raymond mill 12 by 11 storehouses of lignite storage to be crushed, and it is the powder in order to preferably be granulated that lignite, which crushes,
Humic acid in lignite and organic matter after broken can preferably be absorbed by crop, and the lignite after crushing enters activation agitator tank
Activated in 13, activator is entered in activation agitator tank 13 by activator storage tank 14, and lignite activation is in order that in lignite
Reference state humic acid and part free state humic acid be converted to fulvo acid, fulvo acid can be just absorbed by crops
, the utilization rate for fertilizer nutrient using ensuing crop can be improved, the lignite after activation is stirred by measuring belt into disk
Mix in machine 41；
Inorganic component includes a great number of elements and trace element, and each a great number of elements is stored in an a great number of elements warehouse 21
Interior, each trace element is stored in a micro- warehouse 22, according to ratio requirement, in each a great number of elements warehouse 21
Trace element in a great number of elements and each micro- warehouse 22 is entered in pulverizer 24 by measuring belt to be crushed, inorganic
It is to preferably be granulated that component, which crushes, improves granulating rate, and the solid material after crushing enters in disk mixer 41；
Liquid material is glutamic acid mother liquor, and the glutamic acid mother liquor being stored in glutamic acid mother liquor storage tank 31 can enter concentration tank
Concentrated in 32, concentrated liquid material is sticky in order to improve its, while improves its content of organic matter, the glutamic acid after concentration
Mother liquor is entered in disk mixer 41 by flowmeter；
According to ratio requirement, it is mixed that the solid material after lignite and crushing after activation enters stirring in disk mixer 41
Close, meanwhile, the glutamic acid mother liquor after concentration is sprayed in mixing inorganic component, to form mixing wet feed；Mixing wet feed passes through defeated
Send band to enter in granulating disc 42 to be granulated, the wet feed grain after granulation is entered in dryer 43 by conveyer belt dries, and dries
The siccative near 2-3% of grain moisture after dry, entered by conveyer belt in cooler 44 cooled down afterwards, it is dry after cooling
Material grain temperature is down to 10-30 DEG C, is entered by conveyer belt in two level screening machine 45 sieved afterwards, and the two of two level screening machine 45
Level sieve oversize is finished product, and finished product is delivered to finished product bin 5 and stored；It is unqualified that one-level, which sieves oversize and two level sieve screenings,
Product, it is back to by conveyer belt in returning charge tank 46, is delivered in pulverizer 24 is crushed by conveyer belt afterwards, the mesh of screening
Be in order that finished product meets the requirement of relevant national standard, while defective work is separated with finished product, reduce disqualification rate, together
When can improve the utilization rate of material, reduce material waste.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements made etc., the utility model should be included in
Protection domain within.
Claims (5)
1. the production system of the carbon-based compound organic and inorganic fertilizer of biology, it is characterised in that it includes lignite supply system, inorganic component
Supply system, liquid material supply system and system of processing, the discharging opening of the activation agitator tank of the lignite supply system pass through
Measuring belt is connected with the charging aperture of the disk mixer of the system of processing, the pulverizer of the inorganic component supply system
Discharging opening is connected by measuring belt with the charging aperture of the disk mixer of the system of processing, the liquid material supply
The outlet of the concentration tank of system is connected by flowmeter with the inlet of the granulating disc of the system of processing.
2. the production system of the carbon-based compound organic and inorganic fertilizer of biology according to claim 1, it is characterised in that the lignite
Supply system include lignite warehouse, Raymond mill, it is described activation agitator tank, activator storage tank, the discharging opening of the lignite warehouse with
The charging aperture connection of the Raymond mill, the discharging opening of the Raymond mill connect with the charging aperture of the activation agitator tank, the work
The activator inlet communication of the discharging opening of agent storage tank and the activation agitator tank.
3. the production system of the carbon-based compound organic and inorganic fertilizer of biology according to claim 1, it is characterised in that described inorganic
Component supply system includes several a great number of elements warehouses, several micro- warehouses, main conveyor belt and the pulverizer, often
The discharging opening of the individual a great number of elements warehouse is connected by measuring belt with the conveying initiating terminal of the main conveyor belt, Mei Gesuo
The discharging opening for stating micro- warehouse is connected by measuring belt with the conveying initiating terminal of the main conveyor belt, the main conveying
The conveying end of band is placed in the charging aperture of the pulverizer；The liquid material supply system include glutamic acid mother liquor storage tank and
The concentration tank, the outlet of the glutamic acid mother liquor storage tank pass through pipeline and the inlet communication of the concentration tank.
4. the production system of the carbon-based compound organic and inorganic fertilizer of biology according to claim 1, it is characterised in that the processing
System includes the disk mixer, the granulating disc, dryer, cooler, two level screening machine and returning charge tank, the circle
The discharging opening of disk mixer is connected by conveyer belt with the charging aperture of the granulating disc, the discharging opening of the granulating disc
It is connected by conveyer belt with the charging aperture of the dryer, the discharging opening of the dryer is sieved by conveyer belt and the two level
The charging aperture connection of machine, the one-level sieve oversize outlet and the outlet of two level sieve screenings of the two level screening machine pass through conveying respectively
Band is connected with the charging aperture of the returning charge tank, and the two level sieve oversize outlet of the two level screening machine passes through conveyer belt and finished product material
Storehouse connects, and the discharging opening of the returning charge tank passes through conveyer belt and the charging aperture of the pulverizer of the inorganic component supply system
Connection.
5. according to the production system of any described biological carbon-based compound organic and inorganic fertilizers of claim 1-4, it is characterised in that institute
The air outlet for stating granulating disc is connected by pipeline with the air inlet of deduster.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720979455.1U CN207047121U (en) | 2017-08-07 | 2017-08-07 | The production system of the carbon-based compound organic and inorganic fertilizer of biology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720979455.1U CN207047121U (en) | 2017-08-07 | 2017-08-07 | The production system of the carbon-based compound organic and inorganic fertilizer of biology |
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| Publication Number | Publication Date |
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| CN207047121U true CN207047121U (en) | 2018-02-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720979455.1U Active CN207047121U (en) | 2017-08-07 | 2017-08-07 | The production system of the carbon-based compound organic and inorganic fertilizer of biology |
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| Country | Link |
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| CN (1) | CN207047121U (en) |
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2017
- 2017-08-07 CN CN201720979455.1U patent/CN207047121U/en active Active
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