CN110627581A - Compound fertilizer and drying-free production process thereof - Google Patents
Compound fertilizer and drying-free production process thereof Download PDFInfo
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- CN110627581A CN110627581A CN201910932060.XA CN201910932060A CN110627581A CN 110627581 A CN110627581 A CN 110627581A CN 201910932060 A CN201910932060 A CN 201910932060A CN 110627581 A CN110627581 A CN 110627581A
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- air drying
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 54
- 150000001875 compounds Chemical class 0.000 title claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 26
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims abstract description 54
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims abstract description 27
- 235000019341 magnesium sulphate Nutrition 0.000 claims abstract description 27
- 239000003895 organic fertilizer Substances 0.000 claims abstract description 26
- 239000002994 raw material Substances 0.000 claims abstract description 23
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 9
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 claims abstract description 9
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims abstract description 9
- 235000011130 ammonium sulphate Nutrition 0.000 claims abstract description 9
- 239000004202 carbamide Substances 0.000 claims abstract description 9
- 235000019837 monoammonium phosphate Nutrition 0.000 claims abstract description 9
- 239000006012 monoammonium phosphate Substances 0.000 claims abstract description 9
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims abstract description 9
- 229910052939 potassium sulfate Inorganic materials 0.000 claims abstract description 9
- 235000011151 potassium sulphates Nutrition 0.000 claims abstract description 9
- 238000007605 air drying Methods 0.000 claims description 158
- 239000000463 material Substances 0.000 claims description 54
- 238000003860 storage Methods 0.000 claims description 28
- 238000002156 mixing Methods 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 14
- 238000005469 granulation Methods 0.000 claims description 13
- 230000002093 peripheral effect Effects 0.000 claims description 13
- 239000008187 granular material Substances 0.000 claims description 12
- 238000012216 screening Methods 0.000 claims description 12
- 238000007664 blowing Methods 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 11
- 230000003179 granulation Effects 0.000 claims description 7
- 239000000843 powder Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 6
- 238000004806 packaging method and process Methods 0.000 claims description 6
- 238000005096 rolling process Methods 0.000 claims description 6
- 239000011573 trace mineral Substances 0.000 claims description 6
- 235000013619 trace mineral Nutrition 0.000 claims description 6
- 210000001503 joint Anatomy 0.000 claims description 5
- 108090000765 processed proteins & peptides Proteins 0.000 claims description 5
- 239000000440 bentonite Substances 0.000 claims description 4
- 229910000278 bentonite Inorganic materials 0.000 claims description 4
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims description 4
- 238000001125 extrusion Methods 0.000 claims description 3
- 238000009958 sewing Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 241000512259 Ascophyllum nodosum Species 0.000 claims 1
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 description 12
- 239000002689 soil Substances 0.000 description 12
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 9
- 235000017491 Bambusa tulda Nutrition 0.000 description 9
- 241001330002 Bambuseae Species 0.000 description 9
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 9
- 239000011425 bamboo Substances 0.000 description 9
- 235000015097 nutrients Nutrition 0.000 description 7
- 230000001276 controlling effect Effects 0.000 description 6
- 239000006260 foam Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000003245 coal Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000003466 welding Methods 0.000 description 4
- 201000010099 disease Diseases 0.000 description 3
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000011651 chromium Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000575 pesticide Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 description 2
- 229910001950 potassium oxide Inorganic materials 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 241000244203 Caenorhabditis elegans Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 206010010904 Convulsion Diseases 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 230000036461 convulsion Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- YWEUIGNSBFLMFL-UHFFFAOYSA-N diphosphonate Chemical compound O=P(=O)OP(=O)=O YWEUIGNSBFLMFL-UHFFFAOYSA-N 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005706 microflora Species 0.000 description 1
- 235000021048 nutrient requirements Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- -1 pH value Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- DLYUQMMRRRQYAE-UHFFFAOYSA-N phosphorus pentoxide Inorganic materials O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B7/00—Fertilisers based essentially on alkali or ammonium orthophosphates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/30—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotary or oscillating containers; with movement performed by rotary floors
- F26B17/34—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rotary or oscillating containers; with movement performed by rotary floors the movement being in a vertical or steeply inclined plane
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/08—Granular materials
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Fertilizers (AREA)
Abstract
The invention discloses a compound fertilizer and a drying-free production process thereof, wherein the compound fertilizer is mainly prepared from the following raw materials in parts by weight: 300-450 parts of organic fertilizer, 100-200 parts of urea, 100-150 parts of ammonium sulfate, 50-100 parts of monoammonium phosphate, 40-80 parts of potassium sulfate and 100-150 parts of magnesium sulfate. The invention not only simplifies the flow, reduces the equipment investment, but also reduces the environmental pollution.
Description
Technical Field
The invention relates to the technical field of compound fertilizer and bio-organic fertilizer granulation preparation, and particularly relates to a compound fertilizer and a drying-free production process thereof.
Background
Fertilization is the most effective way to increase crop yield. The research shows that the organic fertilizer or functional biological organic fertilizer can not only obviously improve the soil biological activity, but also play an outstanding role in regulating and controlling healthy soil microflora and preventing and controlling soil-borne diseases. The organic wastes are changed into pollution sources to serve as nutrient resources, scientific and reasonable organic fertilizer and inorganic fertilizer proportion is explored to form a refined organic fertilizer or a functional biological organic fertilizer, so that the purposes of reducing weight, improving efficiency and improving the efficient utilization of the nutrient resources are achieved, and key problems of promoting inorganic materials by organic matters, improving the utilization rate of chemical fertilizers, constructing a healthy soil microbial community, reducing soil-borne diseases, improving the sustainable utilization of soil and the like are also concerned. However, according to investigation, the amount of the homogenized fertilizer per mu in China is 21.9 kg, which is far higher than the average level (8 kg per mu) in the world, and is 2.6 times of that in the United states and 2.5 times of that in European Union, and problems of excessive application and blind application of chemical fertilizers and the like bring about cost increase and environmental pollution. The soil hardening and acidification are caused by the large-scale application of the fertilizer, the soil is unhealthy, the unhealthy soil causes crop diseases and causes unhealthy plants, and the unhealthy plants need to be sprayed with pesticide; the pesticide reduces and even kills a plurality of microorganisms and floras in the soil, and a plurality of biological processes in the soil are slowed down or stopped, so that organic matters and beneficial microorganisms in the soil are greatly reduced, and the soil fertility is seriously exhausted.
In the prior art, compound fertilizer burns out the heat-up to the drying furnace before other processes do not start, and the stove internal temperature reaches 400 ℃, and the air outlet temperature reaches within 100 ℃, and in the material sent into the drying furnace through the conveyer belt after mixing, pelletization, start the hot-blast furnace and rotate about 30 minutes, hot-blast furnace start exhaust system simultaneously, semi-manufactured goods flow out from the air outlet and get into next conveying system. However, due to the environmental protection standard, the coal is not allowed to be used for boiler combustion, and is changed into biomass combustion, so that the cost is multiplied, and the secondary pollution to different degrees is caused to the environment due to the fact that the chemical fertilizer gas smell after high temperature is emitted in the drying process.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide a compound fertilizer and a drying-free production process thereof.
In order to achieve the purpose, the invention adopts the technical scheme that: a compound fertilizer is mainly prepared from the following raw materials in parts by weight: 300-450 parts of organic fertilizer, 100-200 parts of urea, 100-150 parts of ammonium sulfate, 50-100 parts of monoammonium phosphate, 40-80 parts of potassium sulfate and 100-150 parts of magnesium sulfate.
Further, the raw materials of the compound fertilizer also comprise: 5-50 parts of sea foam powder.
Further, the raw materials of the compound fertilizer also comprise: 3-20 parts of medium trace elements.
Further, the raw materials of the compound fertilizer also comprise: 5-50 parts of peptide.
Further, the raw materials of the compound fertilizer also comprise: 5-80 parts of bentonite.
Further, the organic fertilizer comprises fully decomposed organic fertilizer which meets the national standard, and the water content is lower than 20%.
Further, the compound fertilizer is prepared from the following raw materials in parts by weight: 428 parts of organic fertilizer, 167 parts of urea, 130 parts of ammonium sulfate, 88 parts of monoammonium phosphate, 67 parts of potassium sulfate, 80 parts of magnesium sulfate, 5 parts of sea foam powder, 20 parts of medium trace elements, 10 parts of peptide and 5 parts of bentonite which meet the standard.
The invention provides another technical scheme that the drying-free production process of the compound fertilizer comprises the following steps:
(1) crushing and mixing raw materials: independently crushing and screening the organic fertilizer, metering and distributing according to a formula proportion, mixing and crushing the other raw materials except the organic fertilizer and magnesium sulfate according to the formula proportion, adding 2/3 magnesium sulfate during mixing and crushing, and finally mixing and uniformly stirring the crushed organic fertilizer and the materials obtained by mixing and crushing to obtain a mixture;
(2) granulating and screening: adding the mixture obtained in the step (1) into an extrusion granulator for granulation, separating granular materials from powdery materials through screening equipment, returning the powdery materials to the granulation equipment for re-granulation, and allowing the granular materials to enter the next process;
(3) primary air drying: conveying the granular materials obtained in the step (2) to a first air drying cylinder body of a special natural air drying device for compound fertilizer production by a conveyor, adding the residual 1/3 magnesium sulfate into the first air drying cylinder body, starting the first air drying cylinder body to rotate and roll, scattering the materials to ensure that the magnesium sulfate can completely wrap and adsorb the materials, simultaneously starting an air blowing system of the first air drying cylinder body, blowing natural air in real time to take away partial moisture of the materials while the materials roll and scatter, reducing the moisture content, and controlling the moisture content of the granular materials within 14%;
(4) and (5) air drying again: feeding the materials processed in the step (3) into a second air drying cylinder body for rotary rolling, throwing the materials to ensure that magnesium sulfate can completely wrap and adsorb the materials, simultaneously starting a blowing system of the second air drying cylinder body, and in the rotary material throwing process, under the action of blowing, enabling the materials to rapidly flow at natural wind speed, reducing the moisture of the materials again to reach the national standard and effectively controlling the moisture of the materials to be below 12%;
(5) screening and packaging: and (5) conveying the materials processed in the step (4) to a rolling sieve through a conveying system, and conveying the screened finished products to a metering hopper through the conveying system, wherein the standard of the finished products is as follows: 3.35-5.6mm, conveying the undersize product which does not meet the standard into a granulator by a conveying system for re-granulation, packaging and metering finished products, and sewing the packages, thereby completing the production process.
Preferably, the first air dryer cylinder has a length of 20 m and a diameter of 1.8 m, and the rotation time of 30 minutes is reached from the beginning of feeding to the end of discharging.
Preferably, the second air dryer cylinder has a length of 20 m and a diameter of 1.5 m, and the feeding from the first air dryer to the discharging takes 30 min rotation time.
Preferably, the natural air drying equipment for producing the compound fertilizer comprises a base, a first air drying cylinder body and a second air drying cylinder body which are fixed on the base in parallel, and is characterized in that,
the feeding end of the first air drying cylinder body is fixedly provided with a hollow first feeding connector through a bearing, the top of the first feeding connector is fixedly provided with a first air drying cylinder feeding hopper, the first air drying cylinder feeding hopper and the first air drying cylinder feeding hopper are communicated, one end, far away from the first air drying cylinder body 1, of the first feeding connector is fixedly provided with a first natural air supply pipeline communicated with the inside of the first air drying cylinder body, the first natural air supply pipeline is connected with a first air blower, the discharging end of the first air drying cylinder body is connected with a temporary storage box through a bearing, the height of the bottom in the temporary storage box is lower than that of the discharging port of the first air drying cylinder body, one end of a scraper conveyor is fixedly arranged in the temporary storage box, a feeding port is formed in the position, corresponding to the bottom in the temporary storage box, of the scraper conveyor for feeding materials to enter the scraper conveyor, and a discharging port is formed in the bottom of one end;
a hollow second feeding joint is fixed at the feeding end of the second air drying cylinder body through a bearing, a second air drying cylinder feeding hopper inclining upwards is fixed at the top of one side of the second feeding joint and communicated with the second air drying cylinder feeding hopper, a second natural air supply pipeline communicated with the inside of the second air drying cylinder body is fixed at one end of the second feeding joint, which is far away from the second air drying cylinder body, and is positioned below the second air drying cylinder feeding hopper, a second air blower is connected with the second natural air supply pipeline, the top opening of the feeding hopper of the second air drying cylinder body is connected and communicated with a discharge hole of a scraper conveyor, and a discharge pipeline is connected and communicated with the discharge end of the second air drying cylinder body;
spiral material raising plates used for conveying materials are welded on the inner wall of the first air drying cylinder body and the inner wall of the second air drying cylinder body;
at least two annular bulges are fixed on the peripheral wall of the first air drying cylinder body and the peripheral wall of the second air drying cylinder body, at least two groups of carrier rollers are fixed on the corresponding base positions of the first air drying cylinder body and the second air drying cylinder body, each annular bulge is matched with the corresponding group of carrier rollers, and the first air drying cylinder body and the second air drying cylinder body are supported on the base through the carrier rollers;
fluted discs are fixed on the peripheral wall of the first air drying cylinder body and the peripheral wall of the second air drying cylinder body, each fluted disc is meshed with a gear driven by a motor output shaft, and the first air drying cylinder body and the second air drying cylinder body are finally driven to rotate through a motor.
Preferably, the first air drying cylinder body and the second air drying cylinder body are formed by butting at least two sections of cylinder bodies, one section of the multi-section cylinder bodies forming the first air drying cylinder body and the second air drying cylinder body is a fixed cylinder body, and the other sections of the multi-section cylinder bodies are movable cylinder bodies, wherein at least one annular bulge is fixed on the outer peripheral wall of each section of movable cylinder body and is supported on a position corresponding to the base by at least one group of carrier rollers; correspondingly, the base is also divided into a fixed base part and a movable base part, wherein the bottom of the movable base part is provided with a sliding groove, correspondingly, a sliding rail which is in sliding fit with the sliding groove on the movable base part is fixed at a corresponding position on the ground, and the movable barrel part is supported on the corresponding movable base part.
Preferably, the movable base part drives the movable base part to slide back and forth on the sliding rail through the telescopic cylinder.
Preferably, the spiral lifting blades welded on the inner wall of the first air drying cylinder and the inner wall of the second air drying cylinder are arranged on the corresponding inner walls of the cylinders along the feed end to the discharge end, and the top of each spiral lifting blade is spaced from the central axis of the cylinder, wherein the top of each spiral lifting blade is the end close to the central axis of the cylinder, and the bottom of each spiral lifting blade is the inner wall of the cylinder for fixing the spiral lifting blade.
Compared with the prior art, the invention has the beneficial effects that:
1. the invention can improve the yield and the quality, does not need the traditional coal drying process, not only simplifies the flow, reduces the equipment investment, but also reduces the environmental pollution;
2. the invention reduces the production cost and labor cost, wherein the cost of the fire coal used in the traditional process comprises the production cost of 40 yuan per ton and the original water loss (the national standard water content is 12 percent, the actual water content is only about 7 percent through the traditional high-temperature quick drying, and the actual water content is calculated according to 2500 yuan per ton, and the 7 percent is 125 yuan), and the original quality nutrient loss (if the original scheme is used for production, the nutrient with the formula higher than 1 percent of the standard point must be designed, and the nutrient is 50 yuan/ton according to the industry standard, and the power consumption of the original coal-fired induced draft fan (22 KW/induced draft fan, the daily power consumption is 176KW calculated according to 8 hours per day, the power consumption per degree is 0.8 yuan, and the daily power consumption is 140 yuan), after the new process is adopted, the fire coal is completely cancelled, the cost can be reduced by about 215 yuan/ton per ton, the production capacity can be calculated according to 4000 tons all year round, and about 86 ten thousand yuan can be saved each year;
3. the fertilizer has comprehensive fertilizer effect elements, is suitable for the nutrient requirements of crops at each growth stage, has lasting and stable fertilizer effect, improves the use efficiency of the fertilizer, improves the physical and chemical properties of soil, and improves the quality and the yield of the crops;
4. the special natural air drying equipment for producing the compound fertilizer has reasonable structural design and small occupied area, and can effectively and fully wrap and adsorb the granular fertilizer and the magnesium sulfate, and the magnesium sulfate adsorbs water in the granular fertilizer; in addition, the first air drying cylinder body and the second air drying cylinder body are arranged into a plurality of sections, and when the inner wall of the air drying cylinder body needs to be cleaned, the movable cylinder body is moved away, so that the air drying cylinder is convenient to clean.
Drawings
FIG. 1 is a process flow diagram relating to the present invention
FIG. 2 is a schematic structural view of the present invention;
FIG. 3 is a cross-sectional view of the first air dryer tube body of the present invention
FIG. 4 is a schematic view showing the connection between the positions of the deposit box and the scraper conveyor according to the present invention
FIG. 5 is a schematic top view of the first and second air dryer cylinders of the present invention in a combined configuration;
FIG. 6 is a schematic top view of the first and second air dryer cylinders of the present invention in a separated configuration;
fig. 7 is a schematic view showing a butt joint state of two sections of the first and second seasoning cylinder bodies according to the present invention;
fig. 8 is a schematic view of the state of the helical material raising plate of the present invention on the inner wall of the first air drying cylinder body or the second air drying cylinder body.
Detailed Description
The invention will now be described in detail with reference to the drawings and specific embodiments.
Preparation of the device:
referring to fig. 1-7, the invention provides a natural air drying device for compound fertilizer production, which comprises a base 1, and a first air drying cylinder body 2 and a second air drying cylinder body 3 which are fixed on the base in parallel, wherein:
the first air drying cylinder barrel 2 is provided with a first feeding joint 14 at the feeding end, the first feeding joint 14 is hollow and provided with a feeding port at one end, the other end is provided with an air inlet port, the top is provided with a feeding port, the first feeding joint 14 is fixed on the base 1 through bolts, one end of the first air drying cylinder barrel 2 is inserted into the feeding port of the first feeding joint 14 and is fixed with a sealing bearing at the connecting part of the first air drying cylinder barrel and the first air drying cylinder barrel (namely, the sealing bearing is embedded into the feeding port and is fixed on the inner wall of the feeding port through a flat plate key, one end of the first air drying cylinder barrel 2 is inserted into the sealing bearing and is fixed on a rotating inner ring of the sealing bearing through a flat plate key), the feeding port of the first feeding joint 14 is fixed with a first air drying cylinder barrel feeding hopper 2.1 through bolts, the bottom outlet of the first air drying cylinder feeding hopper 2.1 is communicated with the inner cavity of the first air drying cylinder barrel 2, and the air inlet port of the first feeding joint 14 of the 2, the first natural air supply pipeline is connected with a first air blower 4 in a conventional mode, the discharge end of the first air drying cylinder body 2 is fixed on the temporary storage box 5 through another sealing bearing (namely, the opening at one side of the temporary storage box 5 is provided, the sealing bearing is embedded into the opening of the temporary storage box and is fixed at the opening through a flat key, the discharge end of the first air drying cylinder body 2 is inserted into the sealing bearing and is fixed with the rotating inner ring of the sealing bearing through the flat key), the discharge port 2.4 of the first air drying cylinder body 2 is positioned in the temporary storage box 5 and is communicated with the temporary storage box 5, the bottom of the temporary storage box 5 is lower than the discharge port of the first air drying cylinder body 2 (preferably, the discharge port of the first air drying cylinder body 2 is arranged at the top of one side of the temporary storage box 5), the bottom of the temporary storage box 5 is cone-shaped, and granular fertilizer in the temporary storage box 5 is conveyed to the second air drying cylinder body 3 through a conveyor, in this application, the conveyor may be a conventional scraper conveyor, if the scraper conveyor is a scraper conveyor, one end of a scraper conveyor 6 is fixed at the bottom of the temporary storage box 5, the scraper conveyor 6 includes a housing 6.1, a scraper conveyor belt 6.2 in the housing 6.1, a driving roller 6.3 for driving the scraper conveyor belt 6.2 to convey, and a driven roller 6.4, a feed port 6.5 is opened on the housing 6.1 corresponding to the bottom of the temporary storage box 5 for feeding granular fertilizer from the temporary storage box 5 into the scraper conveyor 6, a discharge port 6.6 is opened at the bottom of the housing 6.1 far from the feed port, wherein the temporary storage box 5 is opened at one side with a hole for the scraper conveyor 6 to extend into, the corresponding part of the housing 6.1 of the scraper conveyor 6 is sealed and fixed with the hole of the temporary storage box by welding, two ends of the driven roller 6.4 are fixed at the corresponding inner wall position of the temporary storage box 5 by a rotating bearing, one end of a driving roller 6.3 is fixed on a corresponding bracket through a rotating bearing and a bearing seat, the other end of the driving roller 6.3 is fixed with a conveying driving motor through a key, a scraper conveyer belt 6.2 with scrapers is wound on the driving roller and a driven roller 6.4 to form a finished annular conveyer belt, a plurality of vertical scrapers which are fixed at equal intervals on the scraper conveyer belt 6.2 are attached to corresponding positions of the inner wall of a shell 6.1 and are also attached to the inner wall of one side of a temporary storage box and the inner bottom when the scraper conveyer belt runs to the inner bottom of the temporary storage box 5, and the scraper conveyer in the application preferably runs anticlockwise; of course, the conveyor of the present application may also be other conventional granular fertilizer conveyors in the prior art, and a hole may be formed in the bottom of the temporary storage box, and the hole is connected to the top of one side of the granular fertilizer conveyor.
The feeding end of the second air drying cylinder body 3 is also provided with a second feeding joint 15, the structure of the second feeding joint is the same as that of the first feeding joint 14 except that the feeding hole is arranged at the top of one side of the second feeding joint, the connection mode of the second air drying cylinder body 3 and the second feeding joint 1 is the same as that of the first air drying cylinder body and the first feeding joint (connected through a bearing), the feeding hopper 3.1 of the second air drying cylinder is in an inclined shape, the feeding hopper 3.1 of the second air drying cylinder is also fixed or welded on the feeding hole of the second feeding joint through a bolt, the opening at the top of the feeding hopper 3.1 of the second air drying cylinder body 7 is connected and communicated with the discharging hole 6.6 of the scraper conveyor 6, a second natural air supply pipeline communicated with the inside of the second air drying cylinder body 3 is fixed at the feeding end of the second air drying cylinder body 3 and below the feeding hopper 3.1 of the second air drying cylinder body, and the air inlet of the second feeding joint 15 are welded and fixed, the second natural wind supply pipeline is connected with a second air blower 7 in a conventional mode, the discharge end of the second air drying cylinder body 3 is connected with and communicated with a discharge pipeline 8 (can be a negative pressure pipeline in the prior art, and is not shown in a negative pressure source diagram) through a sealing bearing, namely a bell mouth is welded on the discharge pipeline 8 and is communicated with the same, a sealing bearing is embedded in the inner wall of the bell mouth and is fixed through a flat key, the discharge end of the second air drying cylinder body 3 is inserted into the sealing bearing and is fixed with a rotating inner ring of the sealing bearing through the flat key, and the bottom of the bell mouth is fixed on the base 1 through a support in a bolt fixing mode;
spiral lifting plates 9 for lifting and conveying materials are welded on the inner wall of the first air drying cylinder body 2 and the inner wall of the second air drying cylinder body 3; the arc-shaped spiral lifting plate 9 is arranged along the corresponding feeding end of the first air drying cylinder body 2 to the discharging end, and the feeding end of the second air drying cylinder body 3 is arranged to the discharging end;
at least two annular bulges 10 are welded and fixed on the outer peripheral wall of the first air drying cylinder body 2 and the outer peripheral wall of the second air drying cylinder body 3, and at least two groups of carrier rollers 11 (the carrier rollers 11 comprise carrier roller seats and carrier rollers, wherein the carrier roller seats are fixed on the bases through bolts, the carrier rollers are fixed on the carrier roller seats through shafts and roll and rotate relative to the carrier roller seats, namely, two ends of each shaft are fixed on the carrier roller seats through welding or bolts, and the carrier rollers and the shafts are in rotating fit) are fixed on the corresponding base 1 through bolts, each annular bulge 10 is matched with one group of carrier rollers 11 correspondingly, and the first air drying cylinder body 2 and the second air drying cylinder body 3 are supported on the base 1 through the carrier rollers 11;
still weld on the first air-dry section of thick bamboo barrel 2 periphery wall, the second air-dry section of thick bamboo barrel 3 periphery wall and all be fixed with a fluted disc 12, every fluted disc 12 meshes with the gear that is driven by a motor output shaft mutually, drives gear, fluted disc through respective motor, finally drives first air-dry section of thick bamboo barrel 2, the second air-dry section of thick bamboo barrel 3 rotation.
The first air drying cylinder body 2 and the second air drying cylinder body 3 are formed by butt joint of at least two cylinder body parts (two sections are respectively arranged in the drawing), one section of the multi-section cylinder body parts forming the first air drying cylinder body 2 and the second air drying cylinder body 3 is a fixed cylinder body part 2.2 and 3.2, and the rest is a movable cylinder body part 2.3 and 3.3, the movable cylinder body part is butt joint with the corresponding fixed cylinder body part, wherein at least one annular bulge 10 is fixed on the outer peripheral wall of the movable cylinder body part 2.3 and 3.3 and is supported on the corresponding part of the base 1 by at least one group of carrier rollers 11 (the annular bulge is arranged in the drawing); correspondingly, the base 1 is also divided into a fixed base part 1.1 and a plurality of movable base parts 1.2 (one in the figure), wherein the bottom of the movable base part 1.2 is provided with a sliding groove, correspondingly, two parallel sliding rails 13 which are in sliding fit with the sliding groove on one movable base part 1.2 are fixed at corresponding positions on the ground, and the movable cylinder parts 2.3 and 3.3 are supported on the corresponding movable base part 1.2 and ensure that the movable cylinder parts 2.3 and 3.3 which are positioned in the same row on both the first air drying cylinder 2 and the second air drying cylinder 3 are fixed on the same movable base part 1.2.
The outer end of the movable base part 1.2 is welded on the telescopic rods of the two telescopic cylinders, and the movable base part 1.2 is driven to slide back and forth on the slide rail 13 through the telescopic cylinders, so that the movable cylinder part is driven to be in butt joint with the fixed cylinder part or be separated from the fixed cylinder part. Through adopting two sections structures with the air-dry section of thick bamboo barrel that will correspond, can be when keeping in repair or clearing up air-dry section of thick bamboo barrel inside, separate two sections, it is more convenient to clear up or maintain.
According to needs, can be at the temporary storage roof portion that the 2 discharge ends of first air-drying section of thick bamboo body correspond there is the air exhauster through the bolt fastening, the intake stack of air exhauster stretches into the temporary storage incasement and welds at connection position between them, also is fixed with the air exhauster through the bolt on the upper portion that the bell mouth of the discharge end of second air-drying section of thick bamboo body 3 corresponds the discharge conduit, the air intake welding of air exhauster is on the bell mouth wall and both are linked together. Increase the air current exchange speed that drives the inside and external environment of air-drying section of thick bamboo barrel, in order to place granular fertilizer and be inhaled the convulsions machine, the welding of exhaust fan air intake department in the aforesaid two places has the filter screen.
The first air drying cylinder body is 20 meters long and 1.8 meters in diameter, and the second air drying cylinder body is 20 meters long and 1.5 meters in diameter.
Example one
The compound fertilizer is prepared from the following raw materials in parts by weight: 423 parts of organic fertilizer, 167 parts of urea, 130 parts of ammonium sulfate, 85 parts of monoammonium phosphate, 67 parts of potassium sulfate and 128 parts of magnesium sulfate.
The drying-free production process of the compound fertilizer comprises the following steps:
(1) crushing and mixing raw materials: independently crushing and screening the organic fertilizer, metering and distributing according to a formula proportion, mixing and crushing the other raw materials except the organic fertilizer and magnesium sulfate according to the formula proportion, adding 2/3 magnesium sulfate during mixing and crushing, and finally mixing and uniformly stirring the crushed organic fertilizer and the materials obtained by mixing and crushing to obtain a mixture;
(2) granulating and screening: adding the mixture obtained in the step (1) into an extrusion granulator for granulation, separating granular materials from powdery materials through screening equipment, returning the powdery materials to the granulation equipment for re-granulation, and allowing the granular materials to enter the next process;
(3) primary air drying: conveying the granular materials obtained in the step (2) to a first air drying cylinder body by a conveyor, adding the remaining 1/3 magnesium sulfate into the first air drying cylinder body, starting the first air drying cylinder body to rotate and roll for 30 minutes (3-8 revolutions per minute), scattering the materials to ensure that the magnesium sulfate can completely wrap and adsorb the materials, simultaneously starting an air draft system and an air blast system of the first air drying cylinder body, blowing air in real time when the materials roll and fall, and pumping natural air by the air draft system to take away partial moisture of the materials, reducing the moisture content, and controlling the moisture content of the granular materials within 14%;
(4) and (5) air drying again: feeding the material processed in the step (3) into a second air drying cylinder body for rotating and rolling for 30 minutes (2-5 revolutions per minute), throwing the material to ensure that magnesium sulfate can completely wrap and adsorb the material, simultaneously starting an air exhaust system and an air blowing system of the second air drying cylinder body, and in the rotating material throwing process, under the action of air blowing and air exhaust, rapidly flowing at natural air speed, reducing the moisture of the material again to reach the national standard and effectively controlling the moisture to be below 12%;
(5) screening and packaging: and (5) conveying the materials processed in the step (4) to a rolling sieve through a conveying system, and conveying the screened finished products to a metering hopper through the conveying system, wherein the standard of the finished products is as follows: 3.35-5.6mm, conveying the undersize product which does not meet the standard into a granulator by a conveying system for re-granulation, packaging and metering finished products, and sewing the packages, thereby completing the production process.
Example two
The compound fertilizer is prepared from the following raw materials in parts by weight: 423 parts of organic fertilizer, 167 parts of urea, 130 parts of ammonium sulfate, 85 parts of monoammonium phosphate, 67 parts of potassium sulfate, 128 parts of magnesium sulfate and 30 parts of sea foam powder.
The specific production process is the same as the first embodiment.
EXAMPLE III
The compound fertilizer is prepared from the following raw materials in parts by weight: 423 parts of organic fertilizer, 167 parts of urea, 130 parts of ammonium sulfate, 85 parts of monoammonium phosphate, 67 parts of potassium sulfate, 128 parts of magnesium sulfate, 30 parts of sea foam powder and 20 parts of medium trace elements.
The specific production process is the same as the first embodiment.
Example four
The compound fertilizer is prepared from the following raw materials in parts by weight: 423 parts of organic fertilizer, 167 parts of urea, 130 parts of ammonium sulfate, 85 parts of monoammonium phosphate, 67 parts of potassium sulfate, 128 parts of magnesium sulfate, 30 parts of sea foam powder, 20 parts of medium trace elements and 10 parts of peptide.
The specific production process is the same as the first embodiment.
EXAMPLE five
The compound fertilizer is prepared from the following raw materials in parts by weight: 423 parts of organic fertilizer, 167 parts of urea, 130 parts of ammonium sulfate, 85 parts of monoammonium phosphate, 67 parts of potassium sulfate, 128 parts of magnesium sulfate, 30 parts of sea foam powder, 20 parts of medium trace elements, 10 parts of peptide, 20 parts of bentonite and 40 parts of dolomite.
The specific production process is the same as the first embodiment.
In actual experiments, the inventor designs a comparative example, the specific formula of the comparative example is the same as that of the fifth example, but the process is changed, namely, the magnesium sulfate is added during primary air drying. Finally, the products obtained in the five embodiments and the comparative examples are detected to include total nutrients, total nitrogen, available phosphorus, total potassium oxide, pH value, heavy metal content and the like, and the specific results are as follows:
table one: summary of test results
| Example one | Example two | EXAMPLE III | Example four | EXAMPLE five | Comparative example | |
| Organic matter mass fraction (%) with a standard of not less than 15 | 22 | 18.6 | 21.5 | 17.6 | 15.6 | 20.0 |
| The mass fraction (%) of total nutrients is not less than 25.0 | 25.7 | 25.2 | 25．0 | 25.0 | 25.2 | 25.0 |
| Total nitrogen content (%) as measured at 12.0 or more | 12.1 | 11.9 | 12.2 | 12.2 | 11.5 | 12.0 |
| The content (%) of available phosphorus (phosphorus pentoxide) is not less than 6.0 | 5.8 | 6.0 | 5.8 | 6.3 | 6.8 | 5.8 |
| Total potassium oxide content (%), standard is not less than 7.0 | 7.8 | 7.3 | 7.0 | 6.5 | 6.9 | 7.8 |
| pH (pH) of 5.5-8.0 | 5.9 | 6.59 | 6.0 | 6.0 | 6.0 | 6.0 |
| The proportion (%) of the particle size (1.0-4.75 mm) is more than or equal to 70 | 73 | 80 | 82 | 85 | 86 | 70 |
| Mass fraction (%) of chloride ion, standard is less than or equal to 3.0 | 0.2 | 0.18 | 0.3 | 0.29 | 0.31 | 0.2 |
| The death rate (%) of the roundworm eggs is more than or equal to 95 | Without the occurrence of ascarid eggs | Without the occurrence of ascarid eggs | Without the occurrence of ascarid eggs | Without the occurrence of ascarid eggs | Without the occurrence of ascarid eggs | Without the occurrence of ascarid eggs |
| The number of faecal coliform bacteria (per gram) is less than or equal to 100 | ＜2.0 | ＜3.0 | ＜1.0 | ＜2.0 | ＜1.0 | ＜3.0 |
| Arsenic and the mass fraction (calculated As%) of the compounds thereof are less than or equal to 0.0050 | 0.0003 | 0.0001 | 0.0001 | ＜0.0001 | ＜0.0001 | ＜0.0001 |
| Cadmium and the mass fraction (calculated as Cd percent) of the compound are less than or equal to 0.0010 | 0.00003 | 0.0002 | 0.0001 | ＜0.0001 | ＜0.0001 | ＜0.0001 |
| Lead and the mass fraction (calculated as Pb percent) of the compound are less than or equal to 0.0150 | 0.0004 | 0.0003 | 0.0005 | ＜0.0004 | ＜0.002 | ＜0.002 |
| The mass fraction (calculated as Cr,%) of chromium and the compound thereof is less than or equal to 0.0500 | 0.0009 | 0.0008 | 0.0007 | ＜0.0007 | ＜0.0007 | ＜0.0007 |
| Mercury and its compound mass fraction (calculated as Hg,%) is less than or equal to 0.0005 | 0.00002 | 0.00002 | 0.00001 | ＜0.00001 | ＜0.00001 | ＜0.00001 |
Claims (10)
1. A compound fertilizer is mainly prepared from the following raw materials in parts by weight: 300-450 parts of organic fertilizer, 100-200 parts of urea, 100-150 parts of ammonium sulfate, 50-100 parts of monoammonium phosphate, 40-80 parts of potassium sulfate and 100-150 parts of magnesium sulfate.
2. The compound fertilizer as claimed in claim 1, wherein the raw materials further comprise 5-50 parts of kelp powder.
3. The compound fertilizer as claimed in claim 2, wherein the raw materials further comprise 3-20 parts of medium trace elements.
4. The compound fertilizer as claimed in claim 3, wherein the raw material further comprises 5-50 parts of peptide.
5. The compound fertilizer as claimed in claim 4, wherein the raw material further comprises bentonite 5-80 parts.
6. The drying-free production process of compound fertilizer as claimed in any one of the preceding claims, comprising the steps of:
(1) crushing and mixing raw materials: independently crushing and screening the organic fertilizer, metering and distributing according to a formula proportion, mixing and crushing the other raw materials except the organic fertilizer and magnesium sulfate according to the formula proportion, adding 2/3 magnesium sulfate during mixing and crushing, and finally mixing and uniformly stirring the crushed organic fertilizer and the materials obtained by mixing and crushing to obtain a mixture;
(2) granulating and screening: adding the mixture obtained in the step (1) into an extrusion granulator for granulation, separating granular materials from powdery materials through screening equipment, returning the powdery materials to the granulation equipment for re-granulation, and allowing the granular materials to enter the next process;
(3) primary air drying: conveying the granular materials obtained in the step (2) to a first air drying cylinder body of a special natural air drying device for compound fertilizer production by a conveyor, adding the residual 1/3 magnesium sulfate into the first air drying cylinder body, starting the first air drying cylinder body to rotate and roll, scattering the materials to ensure that the magnesium sulfate can completely wrap and adsorb the materials, simultaneously starting an air blowing system of the first air drying cylinder body, blowing natural air in real time to take away partial moisture of the materials while the materials roll and scatter, reducing the moisture content, and controlling the moisture content of the granular materials within 14%;
(4) and (5) air drying again: feeding the materials processed in the step (3) into a second air drying cylinder body for rotary rolling, throwing the materials to ensure that magnesium sulfate can completely wrap and adsorb the materials, simultaneously starting a blowing system of the second air drying cylinder body, and in the rotary material throwing process, under the action of blowing, enabling the materials to rapidly flow at natural wind speed, reducing the moisture of the materials again to reach the national standard and effectively controlling the moisture of the materials to be below 12%;
(5) screening and packaging: and (5) conveying the materials processed in the step (4) to a rolling sieve through a conveying system, and conveying the screened finished products to a metering hopper through the conveying system, wherein the standard of the finished products is as follows: 3.35-5.6mm, conveying the undersize product which does not meet the standard into a granulator by a conveying system for re-granulation, packaging and metering finished products, and sewing the packages, thereby completing the production process.
7. The drying-free production process of compound fertilizer as claimed in claim 6, wherein the first air drying cylinder has a length of 20 m and a diameter of 1.8 m, and the rotation time from the beginning of feeding to the discharging is up to 30 minutes; the second air drying cylinder body is 20 meters long and 1.5 meters in diameter, and the rotation time of the first air drying cylinder body from feeding to discharging of the first air drying cylinder body is 30 minutes.
8. The drying-free production process of compound fertilizer as claimed in claim 7, wherein the natural air drying equipment for producing the purpose-made compound fertilizer comprises a base, a first air drying cylinder body and a second air drying cylinder body which are fixed on the base in parallel,
the feeding end of the first air drying cylinder body is fixedly provided with a hollow first feeding connector through a bearing, the top of the first feeding connector is fixedly provided with a first air drying cylinder feeding hopper, the first air drying cylinder feeding hopper and the first air drying cylinder feeding hopper are communicated, one end, far away from the first air drying cylinder body 1, of the first feeding connector is fixedly provided with a first natural air supply pipeline communicated with the inside of the first air drying cylinder body, the first natural air supply pipeline is connected with a first air blower, the discharging end of the first air drying cylinder body is connected with a temporary storage box through a bearing, the height of the bottom in the temporary storage box is lower than that of the discharging port of the first air drying cylinder body, one end of a scraper conveyor is fixedly arranged in the temporary storage box, a feeding port is formed in the position, corresponding to the bottom in the temporary storage box, of the scraper conveyor for feeding materials to enter the scraper conveyor, and a discharging port is formed in the bottom of one end;
a hollow second feeding joint is fixed at the feeding end of the second air drying cylinder body through a bearing, a second air drying cylinder feeding hopper inclining upwards is fixed at the top of one side of the second feeding joint and communicated with the second air drying cylinder feeding hopper, a second natural air supply pipeline communicated with the inside of the second air drying cylinder body is fixed at one end of the second feeding joint, which is far away from the second air drying cylinder body, and is positioned below the second air drying cylinder feeding hopper, a second air blower is connected with the second natural air supply pipeline, the top opening of the feeding hopper of the second air drying cylinder body is connected and communicated with a discharge hole of a scraper conveyor, and a discharge pipeline is connected and communicated with the discharge end of the second air drying cylinder body;
spiral material raising plates used for conveying materials are welded on the inner wall of the first air drying cylinder body and the inner wall of the second air drying cylinder body;
at least two annular bulges are fixed on the peripheral wall of the first air drying cylinder body and the peripheral wall of the second air drying cylinder body, at least two groups of carrier rollers are fixed on the corresponding base positions of the first air drying cylinder body and the second air drying cylinder body, each annular bulge is matched with the corresponding group of carrier rollers, and the first air drying cylinder body and the second air drying cylinder body are supported on the base through the carrier rollers;
fluted discs are fixed on the peripheral wall of the first air drying cylinder body and the peripheral wall of the second air drying cylinder body, each fluted disc is meshed with a gear driven by a motor output shaft, and the first air drying cylinder body and the second air drying cylinder body are finally driven to rotate through a motor.
9. The drying-free production process of the compound fertilizer as claimed in claim 8, wherein the first air drying cylinder body and the second air drying cylinder body are formed by butt joint of at least two cylinder body parts, one of the cylinder body parts of the multiple cylinder bodies forming the first air drying cylinder body and the second air drying cylinder body is a fixed cylinder body part, and the other cylinder body part is a movable cylinder body part, wherein at least one annular bulge is fixed on the outer peripheral wall of each movable cylinder body part and is supported on the corresponding part of the base by at least one group of carrier rollers; correspondingly, the base is also divided into a fixed base part and a movable base part, wherein the bottom of the movable base part is provided with a sliding groove, correspondingly, a sliding rail which is in sliding fit with the sliding groove on the movable base part is fixed at a corresponding position on the ground, and the movable barrel part is supported on the corresponding movable base part.
10. The drying-free production process of compound fertilizer as claimed in claim 9, wherein the helical material raising plates welded to the inner walls of the first and second air drying cylinders are disposed along the inner walls of the corresponding cylinders from the feeding end to the discharging end, and the top of the helical material raising plate is spaced from the central axis of the cylinder.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111635280A (en) * | 2020-06-10 | 2020-09-08 | 黑龙江实力农业肥料科技有限公司 | Drying-free fertilizer and manufacturing method thereof |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1559995A (en) * | 2004-03-12 | 2005-01-05 | 张树森 | Process for producing composite manure by non drying physics method |
| CN101718488A (en) * | 2009-10-22 | 2010-06-02 | 盐城市腾达环保设备科技有限公司 | Three-cylinder dryer provided with detachable connecting plate |
| CN104420880A (en) * | 2013-08-27 | 2015-03-18 | 成都众成新型复合材料有限公司 | Negative-pressure air drum system and mounting method thereof |
| CN204574724U (en) * | 2014-08-30 | 2015-08-19 | 昆明景晟生物科技有限公司 | Fertilizer combined type lifting drying plant |
| CN105258470A (en) * | 2015-11-26 | 2016-01-20 | 四川东立科技股份有限公司 | Ferrous sulphate heptahydrate drying system |
| CN205425684U (en) * | 2015-12-17 | 2016-08-03 | 南京得清环境工程有限公司 | Fertilizer is drying equipment against current |
| CN109704866A (en) * | 2019-02-27 | 2019-05-03 | 王永刚 | A kind of preparation method of complex microorganism Controlled Release Fertilizer that improveing soil |
-
2019
- 2019-09-29 CN CN201910932060.XA patent/CN110627581A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1559995A (en) * | 2004-03-12 | 2005-01-05 | 张树森 | Process for producing composite manure by non drying physics method |
| CN101718488A (en) * | 2009-10-22 | 2010-06-02 | 盐城市腾达环保设备科技有限公司 | Three-cylinder dryer provided with detachable connecting plate |
| CN104420880A (en) * | 2013-08-27 | 2015-03-18 | 成都众成新型复合材料有限公司 | Negative-pressure air drum system and mounting method thereof |
| CN204574724U (en) * | 2014-08-30 | 2015-08-19 | 昆明景晟生物科技有限公司 | Fertilizer combined type lifting drying plant |
| CN105258470A (en) * | 2015-11-26 | 2016-01-20 | 四川东立科技股份有限公司 | Ferrous sulphate heptahydrate drying system |
| CN205425684U (en) * | 2015-12-17 | 2016-08-03 | 南京得清环境工程有限公司 | Fertilizer is drying equipment against current |
| CN109704866A (en) * | 2019-02-27 | 2019-05-03 | 王永刚 | A kind of preparation method of complex microorganism Controlled Release Fertilizer that improveing soil |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111635280A (en) * | 2020-06-10 | 2020-09-08 | 黑龙江实力农业肥料科技有限公司 | Drying-free fertilizer and manufacturing method thereof |
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