CN204097359U - A kind of less energy-consumption, high-level efficiency compound manure production equipment - Google Patents
A kind of less energy-consumption, high-level efficiency compound manure production equipment Download PDFInfo
- Publication number
- CN204097359U CN204097359U CN201420614271.1U CN201420614271U CN204097359U CN 204097359 U CN204097359 U CN 204097359U CN 201420614271 U CN201420614271 U CN 201420614271U CN 204097359 U CN204097359 U CN 204097359U
- Authority
- CN
- China
- Prior art keywords
- conveyor
- sieve apparatus
- crusher
- sieve
- inlet end
- 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
Landscapes
- Fertilizers (AREA)
Abstract
The utility model discloses a kind of less energy-consumption, high-level efficiency compound manure production equipment; comprise a crusher and three sieve apparatus; also have the part compositions such as batching metering equipment, tablets press, dryer, cooler, coating machine, finished product metering packaging machine; be connected with lift by conveyor between equipment; the side of tablets press is provided with steam boiler, and dryer inlet end is provided with hotblast stove.Through screening process before material granulation, ensure that the fineness of granulation material, there is granulation balling ratio high, the advantage that macrobead is few.Adopt after drying and carry out the screening of macrobead heat, hot broken flow process, there is crushing effect good, the feature that dust is little.The utility model compound manure production equipment, compared with current compound manure production equipment, has that energy consumption is low, device overall operation load is little, efficiency is high, the feature of production process friendly environment.
Description
Technical field
The utility model relates to a kind of fertiliser production device, is specifically related to a kind of less energy-consumption, high-level efficiency compound manure production equipment.
Background technology
At present; compound manure production equipment of the prior art; material enters a crusher and carries out fragmentation after dosing device metering; material after fragmentation enters granulator granulation; after drier, cooler cooling, scalping screening and dusting cover screening is carried out respectively after granulation; macrobead after scalping returns tablets press together with the pulverulent material of No. two crusher in crushing after dusting cover, and salable product enter coating machine, enter wrapping machine and pack after carrying out anti-caking process.Aforesaid device is connected with lift by conveyor, and is provided with steam boiler, hotblast stove and oven dry, cooling falling dust room.
Above-mentioned compound manure production equipment is the widely used production equipment of China, this device production process is simple, operation is easy to grasp, but it is high to there is system energy consumption, need two powerful crushers, raw material crushing and macrobead fragmentation are not exclusively, in granulation process, material that can not be completely broken can form larger particle, increase the load of dryer and cooler, affect output, and raw material crushing and macrobead can produce a large amount of dust in shattering process after cooling, dust in compound manure production process produces when being all fragmentation substantially, cause production plant environment poor, workman easily suffers from the occupational illness such as pneumoconiosis, this is a great problem of puzzlement compound manure manufacturing enterprise.
Summary of the invention
Problem to be solved in the utility model is, provides that a kind of energy consumption is low, device overall operation load is little, production efficiency is high, the compound manure production equipment of production process friendly environment.
The utility model is achieved through the following technical solutions: a kind of less energy-consumption, high-level efficiency compound manure production equipment, comprise a crusher and three sieve apparatus, batching metering equipment is connected by the inlet end of conveyor with a sieve apparatus, the exit end of a sieve apparatus is connected with the inlet end of crusher by conveyor, the end opening end of a sieve apparatus is connected with the inlet end of tablets press by conveyor, the exit end of crusher is connected with the conveyor between batching metering equipment and a sieve apparatus by conveyor, the exit end of tablets press is connected with the inlet end of dryer by conveyor, tablets press is connected with steam boiler, the inlet end of dryer is provided with hotblast stove, the exit end of dryer is connected with the inlet end of No. two sieve apparatus by a lift, the exit end of No. two sieve apparatus is connected with a conveyor between sieve apparatus and crusher by conveyor, the end opening end of No. two sieve apparatus is connected to the inlet end of cooler by conveyor, the exit end of cooler is connected with the inlet end of No. three sieve apparatus by No. two lifts, the end opening end of No. three sieve apparatus is connected with a conveyor between sieve apparatus and tablets press by conveyor, the exit end of No. three sieve apparatus is connected with the inlet end of coating machine, the exit end of coating machine connects finished product metering packaging machine by conveyor.
A described sifted bore dia≤3.0mm; fines after screening removes granulator granulation; the particle of raw material block and more than diameter 3.0mm enters crusher, proceeds screening process through the crusher in crushing conveyor returned between batching metering equipment and a sieve apparatus.
Carry out heat screening through No. two sieve apparatus after drying materials, No. two sifted bore dia 4.5mm, the macrobead after screening returns a sieve apparatus through crusher in crushing and proceeds screening process, and other material enters cooler and carries out subsequent disposal.
Described dryer is also provided with a falling dust room, cooler is also provided with No. two falling dust room.
The beneficial effects of the utility model are:
1, production equipment overall operation load is little, and efficiency is high, and energy-saving effect is remarkable
Through screening before raw material granulation, the fines after screening removes granulator granulation, ensure that the fineness of granulation material, greatly reduces oarse-grained quantity, reduces the load of dryer.Adopt macrobead heat screening after drying, reduce the load of cooler, improve cooling performance.Because the macrobead produced in granulation process is few, and the macrobead only in broken raw material block and granulation process, therefore, use a crusher just can meet need of production., a conventional composite fertiliser production device for designed capacity 100,000 tons, need two crushers, every platform motor of crusher power is not less than 37Kw, the power of cooler is that 37Kw. the utility model production equipment reduces by a raw material crushing machine, increase a sieve apparatus and two for carrying the conveyor of returning charge, increase power and be no more than 15Kw, cooler power is 30Kw.The utility model, compared with conventional production plant, per hourly economizes on electricity about 29 degree, and economize on electricity about 696 degree every day, energy-saving effect is obvious.
2, production process more friendly environment
A large amount of dust can be produced in compound manure production process, be unfavorable for cleaner production and affect worker health, a great problem of this Shi Kunnao compound manure manufacturing enterprise.Dust is mainly derived from raw material and oarse-grained shattering process, and the utility model is reduced by following three kinds of modes and prevented the generation of dust, makes production process more friendly environment:
A, employing raw material first sieve, and the fines after screening goes granulation, and decrease the macrobead that granulation process produces, the load namely reducing crusher additionally reduces the generation of dust.
The flow process of heat screening, heat fragmentation is carried out in b, employing after drying, its benefit is the humidity utilizing macrobead self, thus the dust quantity produced when reducing broken.
The macrobead produced in the raw material block that c, a system crushing and screening goes out and granulation process, whole production equipment uses a crusher just can meet need of production, prevents a large amount of dust produced during raw material crushing.
3, improve quality product and output
Product particle is neat, mellow and full, and irregular particle is few, and granulation process is stablized, and the fluctuation of product nutrient is little, and macrobead is few, and finished particle is many, effectively raises quality product and output.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the utility model less energy-consumption, high-level efficiency compound manure production equipment.
Embodiment:
Below in conjunction with accompanying drawing and embodiment, the utility model is described in further detail:
As shown in Figure 1, less energy-consumption of the present utility model, high-level efficiency compound manure production equipment, comprise a crusher and three sieve apparatus, batching metering equipment 1 is connected by the inlet end of conveyor with a sieve apparatus 3, the exit end of a sieve apparatus 3 is connected by the inlet end of conveyor with crusher 15, the end opening end of a sieve apparatus 3 is connected by the inlet end of conveyor with tablets press 6, the exit end of crusher 15 is connected with the conveyor between batching metering equipment 1 and a sieve apparatus 3 by conveyor, the exit end of tablets press 6 is connected by the inlet end of conveyor with dryer 9, tablets press 6 is connected with steam boiler 5, the inlet end of dryer 9 is provided with hotblast stove 8, the exit end of dryer 9 is connected with the inlet end of No. two sieve apparatus 11 by a lift 10, the exit end of No. two sieve apparatus 11 is connected with the conveyor between a sieve apparatus 3 and crusher 15 by conveyor, the end opening end of No. two sieve apparatus 11 is connected to the inlet end of cooler 18 by conveyor, the exit end of cooler 18 is connected with the inlet end of No. three sieve apparatus 20 by No. two lifts 19, the end opening end of No. three sieve apparatus 20 is connected with the conveyor between a sieve apparatus 3 and tablets press 6 by conveyor, the exit end of No. three sieve apparatus 20 is connected with the inlet end of coating machine 21, the exit end of coating machine 21 connects finished product metering packaging machine 23 by conveyor.
A described sieve apparatus 3 sieve diameters≤3.0mm; fines after screening goes tablets press 6 granulation; the particle of raw material block and more than diameter 3.0mm enters crusher 15, proceeds screening process through the crusher 15 fragmentation conveyor returned between batching metering equipment 1 and a sieve apparatus 3.That is; through a sieve apparatus screening before raw material granulation; sieve diameter≤3.0mm; fines after screening removes granulator granulation; the particle of raw material block and more than diameter 3.0mm returns conveyor through crusher in crushing and proceeds screening process, ensure that the fineness of granulation material, prevents due to the incompletely formed macrobead of raw material crushing; reduce the load of dryer, prevent a large amount of dust produced during raw material crushing.
Carry out heat screening through No. two sieve apparatus 11 after drying materials, No. two sieve apparatus 11 sieve diameter 4.5mm, the macrobead after screening returns a sieve apparatus 3 through crusher 15 fragmentation and proceeds screening process, and other material enters cooler 18 and carries out subsequent disposal.Sieve after adopting the broken and cooling of macrobead heat screening after drying, heat, compared with fragmentation, not only decrease the load of cooler, and it is good to have crushing effect, dust is little, and crusher chain wear is little, the advantage of long service life.
For reducing production process to the pollution of surrounding environment, dryer 9 and cooler 18 side are provided with a falling dust room 26 and No. two falling dust room 25, dryer 9 is connected with a falling dust room 26 by pipeline, cooler 18 is connected with No. two falling dust room 25 by pipeline, and a falling dust room 26 and No. two falling dust room 25 are connected to an induced draft fan 27 and No. two induced draft fans 24.
Raw material block and macrobead fragmentation share a crusher, have saved a large amount of energy consumptions., a conventional composite fertiliser production device for designed capacity 100,000 tons, need two crushers, the power of every platform crusher is not less than 37Kw, and the power of cooler is 37Kw.The utility model production equipment reduces by a raw material crushing machine, increases a sieve apparatus and two for carrying the conveyor of returning charge, and increase power and be no more than 15Kw, cooler power is 30Kw.The utility model, compared with conventional production plant, economizes on electricity about 696 degree every day, and monthly can economize on electricity about 2.08 ten thousand degree, energy-saving effect is obvious.
During production, first the raw material needed for produced compound manure is poured into each hopper in batching metering equipment 1, often raw material dosage is planted by conputer controlled by ratio requirement, avoid the uneven of artificial batching, ensure that product nutrient content is stablized, the raw material that proportioning is good is transported to a sieve apparatus 3 by conveyor and carries out screening process, the particle of raw material block and more than diameter 3.0mm is transported to crusher 15 by conveyor and carries out fragmentation, and after broken, material returns a sieve apparatus 3 through conveyor and proceeds screening process.The material of below diameter 3.0mm is transported in tablets press 6 by conveyor and carries out granulation, meanwhile, passes into steam as amount of liquid phase needed for granulating with improve granulation temperature of charge, complete material granulation process by steam boiler 5 in tablets press 6.After granulation, material is transported in dryer 9 by conveyor, in dryer 9, add hot blast by hotblast stove 8 simultaneously, start an induced draft fan 27 simultaneously, by the moisture sucking-off in dryer 9, enter in air through a falling dust room 26, complete drying course, the height according to product nitrogen content determines bake out temperature, the inlet temperature of dryer 9 controls at 450-600 DEG C, and temperature out controls at 70-100 DEG C.Material after oven dry is transported in No. two sieve apparatus 11 through a lift 10 and carries out the screening of macrobead heat, the raw material block of particle under conveyor conveying is sieved with a sieve apparatus 3 of more than diameter 4.5mm carries out break process by crusher 15 together with the particle of more than diameter 3.0mm, the material of below diameter 4.5mm enters in cooler 18 through conveyor and cools, cooling utilizes No. two induced draft fans 24 to be sent into by freezing air in cooler 18 to carry out cold and hot exchange with material, and enter air through No. two falling dust room 25.Cooled material is sent into No. three sieve apparatus 20 through No. two lifts 19 and is carried out fines screening; the fines of below the 2.0mm sieved out is sent in tablets press 6 through conveyor and is continued granulation; the finished particle of more than 2.0mm is delivered in coating machine 21 and is carried out anti-caking process, is then transported in metering packaging machine 23 by conveyor and packs.
Above-described embodiment is only for illustration of technological thought of the present utility model and feature, its object is to enable those skilled in the art understand content of the present utility model and implement according to this, only can not limit the scope of the claims of the present utility model with the present embodiment, namely the equal change that the spirit that all the utility model disclose is done or modification, still drop in the scope of the claims of the present utility model.
Claims (4)
1. a less energy-consumption, high-level efficiency compound manure production equipment, comprise a crusher and three sieve apparatus, it is characterized in that, batching metering equipment (1) is connected by the inlet end of conveyor with a sieve apparatus (3), the exit end of a sieve apparatus (3) is connected by the inlet end of conveyor with crusher (15), the end opening end of a sieve apparatus (3) is connected by the inlet end of conveyor with tablets press (6), the exit end of crusher (15) is connected with the conveyor between batching metering equipment (1) and a sieve apparatus (3) by conveyor, the exit end of tablets press (6) is connected by the inlet end of conveyor with dryer (9), tablets press (6) is connected with steam boiler (5), the inlet end of dryer (9) is provided with hotblast stove (8), the exit end of dryer (9) is connected with the inlet end of No. two sieve apparatus (11) by a lift (10), the exit end of No. two sieve apparatus (11) is connected with the conveyor between a sieve apparatus (3) and crusher (15) by conveyor, the end opening end of No. two sieve apparatus (11) is connected to the inlet end of cooler (18) by conveyor, the exit end of cooler (18) is connected with the inlet end of No. three sieve apparatus (20) by No. two lifts (19), the end opening end of No. three sieve apparatus (20) is connected with the conveyor between a sieve apparatus (3) and tablets press (6) by conveyor, the exit end of No. three sieve apparatus (20) is connected with the inlet end of coating machine (21), the exit end of coating machine (21) connects finished product metering packaging machine (23) by conveyor.
2. less energy-consumption according to claim 1, high-level efficiency compound manure production equipment; it is characterized in that; described sieve apparatus (3) sieve diameter≤3.0mm; fines after screening goes tablets press (6) granulation; the particle of raw material block and more than diameter 3.0mm enters crusher (15), proceeds screening process through crusher (15) the fragmentation conveyor returned between batching metering equipment (1) and a sieve apparatus (3).
3. less energy-consumption according to claim 1, high-level efficiency compound manure production equipment, it is characterized in that, heat screening is carried out through No. two sieve apparatus (11) after drying materials, No. two sieve apparatus (11) sieve diameter 4.5mm, macrobead after screening returns a sieve apparatus (3) through crusher (15) fragmentation and proceeds screening process, and other material enters cooler (18) and carries out subsequent disposal.
4. less energy-consumption according to claim 1, high-level efficiency compound manure production equipment, it is characterized in that, described dryer (9) is also provided with a falling dust room (26), cooler (18) is also provided with No. two falling dust room (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420614271.1U CN204097359U (en) | 2014-10-22 | 2014-10-22 | A kind of less energy-consumption, high-level efficiency compound manure production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420614271.1U CN204097359U (en) | 2014-10-22 | 2014-10-22 | A kind of less energy-consumption, high-level efficiency compound manure production equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204097359U true CN204097359U (en) | 2015-01-14 |
Family
ID=52265804
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420614271.1U Expired - Fee Related CN204097359U (en) | 2014-10-22 | 2014-10-22 | A kind of less energy-consumption, high-level efficiency compound manure production equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204097359U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658690A (en) * | 2018-08-24 | 2018-10-16 | 山东鸿运工程设计有限公司 | A kind of production system and its production method of microbial organic/inorganic compound fertilizer |
| CN115259929A (en) * | 2021-04-29 | 2022-11-01 | 辽宁新绿源肥料高新技术集团有限公司 | Agricultural compound fertilizer proportioning device |
-
2014
- 2014-10-22 CN CN201420614271.1U patent/CN204097359U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108658690A (en) * | 2018-08-24 | 2018-10-16 | 山东鸿运工程设计有限公司 | A kind of production system and its production method of microbial organic/inorganic compound fertilizer |
| CN115259929A (en) * | 2021-04-29 | 2022-11-01 | 辽宁新绿源肥料高新技术集团有限公司 | Agricultural compound fertilizer proportioning device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101538182B (en) | Functional compound fertilizer, production device and preparation method thereof | |
| CN100515703C (en) | General wood substance grain processing technique and system | |
| CN202379903U (en) | Fertilizer production equipment | |
| CN108503440B (en) | Energy-saving production process in production of granular organic fertilizer | |
| CN218884626U (en) | Coal gangue sintering material shaft furnace cooling device | |
| CN204097359U (en) | A kind of less energy-consumption, high-level efficiency compound manure production equipment | |
| CN102963889B (en) | Efficiently environment-friendly graphitization furnace cooling technology | |
| CN101234904A (en) | Method and device for producing semi-dry type ceramic powdery material | |
| CN203886789U (en) | Organic fertilizer drum screening machine | |
| CN103436320B (en) | Process for preparing derived fuel by using high-humidity household garbage as raw material | |
| CN105713698B (en) | A kind of method of afforestation Castoff material energizing | |
| CN105732001B (en) | A kind of method with stainless steel belt type roasting machine pelletizing method production lytag | |
| CN107353033A (en) | A kind of apparatus system of red mud production sintering-expanded haydite | |
| CN209081763U (en) | A kind of compound fertilizer's automatic production line | |
| KR100933762B1 (en) | Recycling device of industrial wastes | |
| CN208804961U (en) | A kind of drying device of crystal type micronutrient supplement | |
| CN207667602U (en) | A kind of process equipment of biological particles | |
| CN207193134U (en) | A kind of Full-automatic lime production line Distributed Control System | |
| CN104927964A (en) | Biomass forming fuel as well as production method and production system thereof | |
| CN103252195A (en) | Fluidized bed granulation system | |
| CN212093099U (en) | Drying and cooling screen integrated machine | |
| CN203999422U (en) | Biological organic granulated fertilizer production line | |
| CN202430141U (en) | Production equipment for compound fertilizers | |
| CN207404843U (en) | A kind of LiFePO4 production equipment | |
| CN206909678U (en) | A kind of fodder production line |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150114 Termination date: 20171022 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |