CN101987795B - Special fertilizer production method and special equipment thereof - Google Patents
Special fertilizer production method and special equipment thereof Download PDFInfo
- Publication number
- CN101987795B CN101987795B CN2010102491264A CN201010249126A CN101987795B CN 101987795 B CN101987795 B CN 101987795B CN 2010102491264 A CN2010102491264 A CN 2010102491264A CN 201010249126 A CN201010249126 A CN 201010249126A CN 101987795 B CN101987795 B CN 101987795B
- Authority
- CN
- China
- Prior art keywords
- machine
- hopper
- fertilizer
- compound
- dryer
- 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.)
- Active
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Fertilizers (AREA)
Abstract
The invention relates to a special fertilizer production method and special equipment thereof, which are mainly used for producing an organic granulated fertilizer and an organic-inorganic mixed granulated fertilizer. The method comprises the following process steps of: mixing, stirring, performing windrow fermentation, turning, decomposing, drying, performing coarse grinding, screening, performing fine grinding and mixing. The drying temperature is controlled to be between 60 and 70 DEG C and the drying humidity is controlled to be 30 to 35 percent in the whole production process, so that most microorganisms can survive, and the biological fertilizer efficiency is obvious. The fertilizer with the moisture content of 30 to 40 percent can be ground by a special fine grinding machine, so that production efficiency is improved by ten times; and the grinding quality of the fertilizer is greatly improved, and the granule size of the ground fertilizer granules can be controlled to be 1mm and below.
Description
(1) technical field
The present invention relates to a kind of dedicated fertilizer production method and specific equipment thereof.Be mainly used in the production of the dedicated fertilizers such as vegetables, fruit tree.
(2) background technology
Fertilizer on the market is divided into special fertilizer, common fertilizer (pulvis), common fertilizer (particle), coat fertilizer and BB fertile (also being Bulk Blending Fertilizer) usually.
The manufacture craft of special fertilizer directly affects production efficiency and the fertilizer quality of fertilizer.Traditional fertilizer manufacture craft is normally: batching → stir → hyperthermia drying (complete drying) → screening → salable product classification packing warehouse-in → unacceptable product → advance to enter the next one after pulverizer is pulverized again and circulate.This kind technique has the following disadvantages:
1, behind the employing hyperthermia drying, microorganism is killed totally substantially in the fertilizer, and this kind fertilizer only rises and loosens the soil, adds organic egency, and simultaneously, by infertile fields such as adding inorganic additivess (N, P, K), the fertilizer effect is very low, serious waste of resources.
Produce a large amount of coarse fodders during 2, owing to the fertilizer screening and need further pulverizing, production efficiency is low, and granulate quality obviously descended when returns was granulated again simultaneously.
3, using the Ordinary pulverization machine, mainly is by ring mill granulation or plain grinding granulation or throwing sieve etc., and passage easily occurs during pulverizing, causes fault shut-down etc., and simultaneously, this technique dust is large, noise is large, and environmental pollution is serious.
(3) summary of the invention
The object of the invention is to overcome above-mentioned deficiency, provide a kind of make microorganism be able to survival, granulate quality and granulation efficient all higher, be difficult for when pulverizing that passage occurs and dust is little, noise is little, dedicated fertilizer production method and the specific equipment thereof of non-environmental-pollution.
The object of the present invention is achieved like this: a kind of dedicated fertilizer production method, and described method comprises following processing step:
The raw material of preparation fertilizer is added mixing machine by proportioning mix, be mixed with compound, the compound moisture control is at 60%-65%,
The compound of step 1 preparation is added stirrer, stirs,
Step 3, the fermentation of bar buttress formula
Compound after step 2 stirs is piled up the slivering buttress, carries out the fermentation of bar buttress formula,
Step 4, turn over throwing
With turnover throwing machine the buttress of the bar after the step 3 fermentation is turned over throwing, turned over throwing once in per 48 hours ± 5 hours, bar buttress temperature is controlled at 65 ℃-70 ℃,
Fermented 15-20 days, compound becomes thoroughly decomposed, and passes through 15-20 days stacking again, carries out after-ripening,
Become thoroughly decomposed, water ratio is transported to the first dryer at the compound of 40%-45%, the first dryer heats with the first hotblast stove, the temperature of the first dryer is controlled at 60 ℃-70 ℃, moisture control is at 30%-35% after the oven dry, the first dryer utilizes the first induced draft fan air inducing, and carry out dedusting, rear discharging up to standard with the first fly-ash separator
Step 7, coarse reduction
Compound after will drying with Roughpulverizer is pulverized,
Carry out thickness with the compound of the first sifting machine after with coarse reduction and separate, the coarse fodder that screens is again got back to Roughpulverizer and is pulverized,
It is broken to utilize fines after slimer will screen to carry out fine powder, and compound length is controlled at below the 1mm after pulverizing,
Compound after fine powder is broken adds the second mixing machine, adds some inorganic additivess by proportioning again, installs electronic scales additional at the second mixing machine, carries out different proportioning weighings, mixes, and mixed finished product through packing, are made special fertilizer.
The specific equipment of dedicated fertilizer production method of the present invention, comprise the first mixing machine, stirrer, turnover throwing machine, transfer roller, the first dryer, Roughpulverizer, the first sifting machine, slimer, the batching delivery system, the second mixing machine and wrapping machine, described the first mixing machine outlet links to each other with stirrer, turnover throwing machine is arranged in the stirrer rear, transfer roller is arranged in the turnover throwing machine rear, conveyor outlet links to each other with the first dryer import, the first dryer heats with the first hotblast stove, the first dryer top is connected with the first air-suction duct, the outlet of the first air-suction duct links to each other with one first fly-ash separator, the first fly-ash separator links to each other with one first induced draft fan, the first induced draft fan links to each other with one first chimney, described the first dryer outlet links to each other with the Roughpulverizer import, the Roughpulverizer outlet links to each other with the first sifting machine import, the outlet of the first sifting machine coarse fodder links to each other with the Roughpulverizer import, the outlet of the first sifting machine fines links to each other with the slimer import, the slimer outlet links to each other with the second mixing machine import, and the second mixing machine import also links to each other with the batching delivery system; The outlet of the second mixing machine links to each other with wrapping machine, and the second mixing machine is with electronic scales.
The specific equipment of dedicated fertilizer production method of the present invention, described slimer comprises a support, and a hopper and a power system are installed on this support, and hopper top is connected with a hopper, and the hopper bottom is discharge port; Described power system comprises power shaft and cutter head assembly, power shaft vertically is inserted in the hopper, cutter head assembly is installed on the interior power shaft of hopper, this cutter head assembly comprises two cutterheads and four blade axle, described two cutterheads are fixedly connected on the power shaft one on the other, the four blade axle is connected between described up and down two cutterheads by thru-bolt, and the four blade axle to be evenly arranged in described power shaft peripheral; On described cutter shaft, evenly be set with from top to bottom the multi-disc blade, and the dislocation of the blade in the vertical direction on two adjacent two cutter shafts layout, and all blades all are horizontally disposed; Corresponding to the cutter head assembly on the described power shaft, be compounded with a gear ring at the inwall of described hopper.
The specific equipment of dedicated fertilizer production method of the present invention is provided with a double wedge in the middle of the outer end of described blade, all be the symmetrical cloth of step in the both sides, outer end of blade and be provided with a plurality of double wedges, and described gear ring is straight trough type gear ring.
The specific equipment of dedicated fertilizer production method of the present invention, described hopper is cylindrical, and the hopper top is provided with a case lid, on one side case lid is provided with a feed port, periphery, the feed port back side is provided with a baffle liner.
The invention has the beneficial effects as follows:
1, whole production process bake out temperature is controlled at 60~70 ℃, and oven dry humidity is controlled at 30%~35%, and most microorganisms are survived, and biological fertilizer efficiency effect is obvious.
2, use special-purpose slimer, the pulverizing of moisture fertilizer and the difficulty of granulating, equipment obstruction shut-down problem have thoroughly been solved, can under fertilizer 30%~40% water ratio, pulverize, 10 times of ground have improved production efficiency, and fertilizer pulverizes quality and be greatly improved, and pulverize fertiliser granulates and can be controlled in 1mm and following, simultaneously, this equipment is to pulverize fertilizer in the container of sealing, has effectively reduced noise, has avoided dust pollution, has improved Working environment.
(4) description of drawings
Fig. 1 is that dedicated fertilizer of the present invention is produced the specific equipment general arrangement.
Fig. 2 is the Facad structure synoptic diagram of slimer of the present invention.
Fig. 3 is the vertical view of Fig. 2.
Fig. 4 is the left side view of Fig. 2.
Fig. 5 is the A-A sectional view of Fig. 3.
Fig. 6 is hopper of the present invention and power system connection diagram.
Fig. 7 is hopper internal structure synoptic diagram of the present invention.
Fig. 8 is the B-B sectional view of Fig. 7.
Fig. 9 is the C-C sectional view of Fig. 7.
Figure 10 is blade running figure of the present invention.
Figure 11 is the I enlarged view of Fig. 9.
Figure 12 is fundamental diagram one of the present invention.
Figure 13 is fundamental diagram two of the present invention.
Figure 14 is the II enlarged view of Figure 13.
Figure 15 is the III enlarged view (dustband enlarged view) of Fig. 7.
Reference numeral among the figure:
The first mixing machine 1, stirrer 2, bar buttress formula fermentation 3, turnover throwing machine 4, become thoroughly decomposed 5, transfer roller 6, the first hotblast stove 7, the first dryer 8, the first air-suction duct 9, the first fly-ash separator 10, the first induced draft fan 11, the first chimney 12, Roughpulverizer 13, the first sifting machine 14, slimer 15, batching delivery system 16, the second mixing machine 17, check 18, wrapping machine 19, warehouse-in 20.
Support 15.1, hopper 15.2, the first web member 15.3, hopper 15.4, the second web member 15.5, power system 15.6, bolt pair 15.7, blade 15.8, gear ring 15.9, fertilizer 15.10;
Case lid 15.2.1, feed port 15.2.1.1, baffle liner 15.2.1.2;
Shield cap 15.6.1, motor 15.6.2, transmission belt 15.6.3, electrical machine belt pulley 15.6.4, driven pulley 15.6.5, power shaft 15.6.6, bearing housing 15.6.7, bearing 15.6.8, cutterhead 15.6.9, cutter shaft 15.6.10;
Double wedge 15.8.1,15.8.2,15.8.3,15.8.4;
Straight trough 15.9.1.
(5) embodiment
Dedicated fertilizer production method of the present invention comprises following technological process:
The raw material of preparation fertilizer is mixed by proportioning (carbon-nitrogen ratio of setting) adding mixing machine, be mixed with compound, the compound moisture control is at 60%-65%.Described raw material packet contains feces of livestock and poultry, stalk, rice chaff, edible fungi residues, food factory's organic waste and bacterial classification, and it is fixed that its proportioning is come by the raw material composition.
The compound of step 1 preparation is added stirrer, stir.
Step 3, the fermentation of bar buttress formula
Compound after step 2 stirs is piled up the slivering buttress, carry out the fermentation of bar buttress formula.
Step 4, turn over throwing
With turnover throwing machine the buttress of the bar after the step 3 fermentation is turned over throwing, play pulverizing, oxygenation, promotion microbial reproduction and the fast effect of volatilization moisture, turned over throwing once in per 48 hours ± 5 hours, bar buttress temperature is controlled at 65 ℃-70 ℃.
Fermented 15-20 days, compound becomes thoroughly decomposed, and passes through 15-20 days stacking again, carries out after-ripening.
Become thoroughly decomposed, water ratio is transported to the first dryer at the compound of 40%-45%, the first dryer heats with the first hotblast stove, the temperature of the first dryer is controlled at 60 ℃-70 ℃ (not affecting the survival temperature of bacterial classification), moisture control is at 30%-35% after the oven dry, the first dryer utilizes the first induced draft fan air inducing, moisture content in the compound after the heating is discharged, and carry out dedusting, rear discharging up to standard with the first fly-ash separator.
Step 7, coarse reduction
Compound is in drying course, and it is agglomerating to lump easily, and the compound after will drying with Roughpulverizer is pulverized.
Carry out thickness with the compound of the first sifting machine after with coarse reduction and separate, the coarse fodder that screens is again got back to Roughpulverizer and is pulverized.
Material is still larger after the screening, does not reach the requirement of granulation, and it is broken to utilize fines after slimer will screen to carry out fine powder, and pulverizing afterwards, compound length is controlled at below the 1mm.
Compound after fine powder is broken adds the second mixing machine, add some inorganic additivess (nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and some trace elements etc.) by proportioning again, install electronic scales additional at the second mixing machine, carry out different proportioning weighings, mix, mixed finished product through the packing storehouse, are made dedicated fertilizer.Referring to Fig. 1, Fig. 1 is organic fertiliser production specific equipment of the present invention, comprise the first mixing machine 1, stirrer 2, turnover throwing machine 4, transfer roller 6, the first dryer 8, Roughpulverizer 13, the first sifting machine 14, slimer 15, batching delivery system 16, the second mixing machine 17 and wrapping machine 19,1 outlet of described the first mixing machine links to each other with stirrer 2, turnover throwing machine 4 is arranged in stirrer 2 rears, transfer roller 6 is arranged in turnover throwing machine 4 rears, transfer roller 6 outlets link to each other with 8 imports of the first dryer, 7 heating of the first dryer 8 usefulness the first hotblast stove, the first dryer 8 tops are connected with the first air-suction duct 9,9 outlets of the first air-suction duct link to each other with one first fly-ash separator 10, the first fly-ash separator 10 links to each other with one first induced draft fan 11, the first induced draft fan 11 links to each other with one first chimney 12,8 outlets of described the first dryer link to each other with Roughpulverizer 13 imports, Roughpulverizer 13 outlets link to each other with 14 imports of the first sifting machine, the outlet of the first sifting machine 14 coarse fodders links to each other with Roughpulverizer 13 imports, the outlet of the first sifting machine 14 fineves links to each other with slimer 15 imports, slimer 15 outlets link to each other with 17 imports of the second mixing machine, and 17 imports of the second mixing machine also link to each other with batching delivery system 16; 17 outlets of the second mixing machine link to each other with wrapping machine 19, and the second mixing machine 17 is with electronic scales.
The present invention utilizes computer system that whole Production Flow Chart is linked up, and carries out computer and controls.
Referring to Fig. 2~4, Fig. 2 is the Facad structure synoptic diagram of slimer of the present invention.Fig. 3 is the vertical view of Fig. 2.Fig. 4 is the left side view of Fig. 2.Can be found out that by Fig. 2, Fig. 3 and Fig. 4 slimer of the present invention comprises a support 15.1, this support 15.1 is equipped with a hopper 15.2 by web member 15.3 on one side, and hopper 15.2 tops are connected with a hopper 15.4, and hopper 15.2 bottoms are discharge port; These support 15.1 the other sides are connected with a power system 15.6 by web member 15.5 and bolt pair 15.7 (quadruplet).
Referring to Fig. 5~6, Fig. 5 is the A-A sectional view of Fig. 3.Fig. 6 is hopper of the present invention and power system connection diagram.Can be found out that by Fig. 5 and Fig. 6 described hopper 15.2 is cylindrical, hopper 15.2 tops are provided with a case lid 15.2.1, on one side case lid 15.2.1 is provided with a feed port 15.2.1.1, the fertilizer in the hopper 15.4 among Fig. 2 can enter in the hopper 15.2 by this hole.Periphery, the feed port 15.2.1.1 back side is provided with the baffle liner 15.2.1.2 that a band steel surrounds.Its III partial enlarged drawing as shown in figure 15.Described power system 15.6 comprises motor 15.6.2, electrical machine belt pulley 15.6.4, transmission belt 15.6.3, driven pulley 15.6.5, power shaft 15.6.6, bearing support 15.6.7, bearing 15.6.8 and cutter head assembly, motor 15.6.2 is installed on the web member 15.5 by bolt pair 15.7 (quadruplet), electrical machine belt pulley 15.6.4 is installed in motor 15.6.2 output terminal, transmission belt 15.6.3 is sleeved on electrical machine belt pulley 15.6.4 and the driven pulley 15.6.5, driven pulley 15.6.5 is installed in power shaft 15.6.6 upper end, and at electrical machine belt pulley 15.6.4, transmission belt 15.6.3, driven pulley 15.6.5 is set with a shield cap 15.6.1 outward.Described power shaft 15.6.6 top is installed in the middle of the described case lid 15.2.1 by bearing support 15.6.7 and bearing 15.6.8, and described bearing support 15.6.7 and bearing 15.6.8 are installed on the case lid 15.2.1 back side, power shaft 15.6.6 bottom vertically is inserted in the hopper 15.2, cutter head assembly is installed on the power shaft 15.6.6 in the hopper 15.2, this cutter head assembly comprises two cutterhead 15.6.9 and four blade axle 15.6.10, described two cutterhead 15.6.9 are fixedly connected on the power shaft 15.6.6 one on the other, four blade axle 15.6.10 is connected between the described up and down two cutterhead 15.6.9 by thru-bolt, and four cutter shaft 15.6.10 to be evenly arranged in described power shaft 15.6.6 peripheral.
Referring to Fig. 7~8, Fig. 7 is hopper internal structure synoptic diagram of the present invention.Fig. 8 is the B-B sectional view of Fig. 7.Can be found out by Fig. 7 and Fig. 8, among described four cutter shaft 15.6.10, have and all evenly be set with from top to bottom five blades 15.8 on two cutter shaft 15.6.10, all evenly be set with from top to bottom four blades 15.8 on two cutter shaft 15.6.10 in addition, and the blade 15.8 in the vertical directions dislocation on two adjacent two cutter shaft 15.6.10 is arranged, and all blades 15.8 all are horizontally disposed.
Referring to Fig. 9, Fig. 9 is the C-C sectional view of Fig. 7.As seen from Figure 9, corresponding to the cutter head assembly on the power shaft 15.6.6, be compounded with a gear ring 15.9 at the inwall of described hopper 15.2.
Referring to Figure 10, Figure 10 is blade running figure of the present invention.As seen from Figure 10, when blade after the position of Fig. 9 starts power system 15.6 runnings, totally 18 blades 15.8 on four cutter shaft 15.6.10 are thrown away at once.
Referring to Figure 11, Figure 11 is the I enlarged view of Fig. 9.As seen from Figure 11, be provided with a double wedge 15.8.1 in the middle of the outer end of described blade 15.8, the both sides, outer end of blade 15.8 all are the symmetrical cloth of step and are provided with three double wedge 15.8.2,15.8.3,15.8.4; Described gear ring 15.9 is straight trough 15.9.1 type gear ring.
Principle of work:
Referring to Figure 12~14, Figure 12 is fundamental diagram one of the present invention.Figure 13 is fundamental diagram two of the present invention.Figure 14 is the II enlarged view of Figure 13.As seen from Figure 12, the feed port 15.2.1.1 that offers on the case lid 15.2.1 by hopper 15.2 after fertilizer 15.10 enters hopper 15.4 enters in the hopper 15.2,18 blades 15.8 in the hopper under the driving of power system 15.6 in hopper high speed rotating, with the fertilizer 15.10 continuous cutting and grinding that enter in the hopper, simultaneously, the particle of fertilizer 15.10 constantly is thrown to around the wall of hopper 15.2, as shown in figure 13, arrive the fertilizer at hopper edge constantly by the double wedge 15.8.1 of blade 15.8,15.8.2,15.8.3,15.8.4 corner angle are pulverized, and be thrown on the gear ring 15.9, under the effect of impact force, constantly broken by the straight trough 15.9.1 corner angle of gear ring 15.9, fertilizer is under gravity and baffle liner effect, constantly broken by the corner angle of the blade 15.8 of different positions and gear ring 15.9 in transmittance process from top to bottom, until reach the standard particle requirement.
In the process that fertiliser granulates is pulverized, be flushed to behind fertilizer on the case lid 15.2.1 of hopper 15.2 and the baffle liner 15.2.1.2 of dust in meeting Fig. 5 by gear feed back case 15.2 inside, make fertiliser granulates and dust not pass hopper and outwards go out, effectively improved Working environment.
Annotate:
Carbon-nitrogen ratio (C/N):
The total content of carbon is called carbon-nitrogen ratio with the ratio of the total content of nitrogen in the organism.
Make in the organic material of compost, the ratio of carbon element and nitrogen, suitable carbon-nitrogen ratio (the suitableeest C/N is 20/1) helps microbial fermentation to decompose.
Adjust carbon-nitrogen ratio: cow dung C/N is 20~23/1, and pig manure is 10~14/1, and chicken manure is 9~10/1, so cow dung can not adjusted C/N during compost treatment, and the pig chicken manure needs; Adjust rice husk (C/N is 70/1), the mushroom class of material high C/N commonly used and discard wood chip (C/N is 57/1) and wood chip (C/N is 298/1) etc.
Special fertilizer:
So-called special fertilizer is exactly the nutrient uptake feature according to regional soil situation and crop, the nutritive elements such as nitrogen, phosphorus, potassium and trace element is carried out scientific matching, for the special fertilizer of this area crops.
Special fertilizer according to the crop growth rule with to the development and production of different element absorption amount, by the analysis to the soil nutrient content characteristics, regulation of fertilizer requirement according to Different Crop, in conjunction with local habits fertilization level, cropping system and natural climate condition, develop various Special Fertilizers for Various Crops Chemical Mixed Fertilizers with suiting measures to local conditions, and for Different Crop, different soils has added various healthy trace elements with household and can promote the pungent of plant growth in fertilizer, " skill thing " adequate and systematic service technology of carrying out simultaneously, so this becomes gradually, and to solve utilization rate of fertilizer low, one of method of the problem such as crop yield and Quality Down.
Claims (5)
1. dedicated fertilizer production method is characterized in that described method comprises following processing step:
Step 1, mixing
The raw material of preparation fertilizer is added mixing machine by proportioning mix, be mixed with compound, the compound moisture control is at 60%-65%,
Step 2, stirring
The compound of step 1 preparation is added stirrer, stirs,
Step 3, the fermentation of bar buttress formula
Compound after step 2 stirs is piled up the slivering buttress, carries out the fermentation of bar buttress formula,
Step 4, turn over throwing
With turnover throwing machine the buttress of the bar after the step 3 fermentation is turned over throwing, turned over throwing once in per 48 hours ± 5 hours, bar buttress temperature is controlled at 65 ℃-70 ℃,
Step 5, become thoroughly decomposed
Fermented 15-20 days, compound becomes thoroughly decomposed, and passes through 15-20 days stacking again, carries out after-ripening,
Step 6, oven dry
Become thoroughly decomposed, water ratio is transported to the first dryer at the compound of 40%-45%, the first dryer heats with the first hotblast stove, the temperature of the first dryer is controlled at 60 ℃-70 ℃, moisture control is at 30%-35% after the oven dry, the first dryer utilizes the first induced draft fan air inducing, and carry out dedusting, rear discharging up to standard with the first fly-ash separator
Step 7, coarse reduction
Compound after will drying with Roughpulverizer is pulverized,
Step 8, screening
Carry out thickness with the compound of the first sifting machine after with coarse reduction and separate, the coarse fodder that screens is again got back to Roughpulverizer and is pulverized,
Step 9, fine powder are broken
It is broken to utilize fines after slimer will screen to carry out fine powder, and compound length is controlled at below the 1mm after pulverizing,
Step 10, batching
Compound after fine powder is broken adds the second mixing machine, adds some inorganic additivess by proportioning again, installs electronic scales additional at the second mixing machine, carries out different proportioning weighings, mixes, and mixed finished product through packing and warehouse-in, are made dedicated fertilizer,
The specific equipment that described method adopts comprises the first mixing machine (1), stirrer (2), turnover throwing machine (4), transfer roller (6), the first dryer (8), Roughpulverizer (13), the first sifting machine (14), slimer (15), batching delivery system (16), the second mixing machine (17) and wrapping machine (19), described the first mixing machine (1) outlet links to each other with stirrer (2), turnover throwing machine (4) is arranged in stirrer (2) rear, transfer roller (6) is arranged in turnover throwing machine (4) rear, transfer roller (6) outlet links to each other with the first dryer (8) import, the first dryer (8) heats with the first hotblast stove (7), the first dryer (8) top is connected with the first air-suction duct (9), the first air-suction duct (9) outlet links to each other with one first fly-ash separator (10), the first fly-ash separator (10) links to each other with one first induced draft fan (11), the first induced draft fan (11) links to each other with one first chimney (12), described the first dryer (8) outlet links to each other with Roughpulverizer (13) import, Roughpulverizer (13) outlet links to each other with the first sifting machine (14) import, the outlet of the first sifting machine (14) coarse fodder links to each other with Roughpulverizer (13) import, the outlet of the first sifting machine (14) fines links to each other with slimer (15) import, slimer (15) outlet links to each other with the second mixing machine (17) import, and the second mixing machine (17) import also links to each other with batching delivery system (16); The second mixing machine (17) outlet links to each other with wrapping machine (19), and the second mixing machine (17) is with electronic scales.
2. a kind of dedicated fertilizer production method according to claim 1, it is characterized in that described slimer (15) comprises a support (15.1), one hopper (15.2) and a power system (15.6) are installed on this support (15.1), hopper (15.2) top is connected with a hopper (15.4), and hopper (15.2) bottom is discharge port; Described power system (15.6) comprises power shaft (15.6.6) and cutter head assembly, power shaft (15.6.6) vertically is inserted in the hopper (15.2), cutter head assembly is installed on the interior power shaft (15.6.6) of hopper (15.2), this cutter head assembly comprises two cutterheads (15.6.9) and four blade axle (15.6.10), described two cutterheads (15.6.9) are fixedly connected on the power shaft (15.6.6) one on the other, four blade axle (15.6.10) is connected between described up and down two cutterheads (15.6.9) by thru-bolt, and four blade axle (15.6.10) is evenly arranged in described power shaft (15.6.6) periphery; On described cutter shaft (15.6.10), evenly be set with from top to bottom multi-disc blade (15.8), and the dislocation of blade (15.8) in the vertical direction on two adjacent two cutter shafts (15.6.10) is arranged, and all blades (15.8) all are horizontally disposed; Corresponding to the cutter head assembly on the described power shaft (15.6.6), be compounded with a gear ring (15.9) at the inwall of described hopper (15.2).
3. a kind of dedicated fertilizer production method according to claim 2, it is characterized in that in the middle of the outer end of described blade (15.8), being provided with a double wedge (15.8.1), all be the symmetrical cloth of step in the both sides, outer end of blade (15.8) and be provided with a plurality of double wedges (15.8.2,15.8.3,15.8.4), described gear ring (15.9) is straight trough (15.9.1) type gear ring.
4. according to claim 2 or 3 described a kind of dedicated fertilizer production methods, it is characterized in that described hopper (15.2) is cylindrical, hopper (15.2) top is provided with a case lid (15.2.1), case lid (15.2.1) is provided with a feed port (15.2.1.1) on one side, and feed port (15.2.1.1) periphery, the back side is provided with a baffle liner (15.2.1.2).
5. a kind of dedicated fertilizer production method according to claim 4, it is characterized in that described power system (15.6) also comprises motor (15.6.2), electrical machine belt pulley (15.6.4), transmission belt (15.6.3) and driven pulley (15.6.5), motor (15.6.2) is installed on the second web member (15.5) by bolt pair (15.7), the second web member (15.5) is installed on the support (15.1), electrical machine belt pulley (15.6.4) is installed in motor (15.6.2) output terminal, transmission belt (15.6.3) is sleeved on electrical machine belt pulley (15.6.4) and the driven pulley (15.6.5), driven pulley (15.6.5) is installed in power shaft (15.6.6) upper end, and at electrical machine belt pulley (15.6.4), transmission belt (15.6.3), the outer shield cap (15.6.1) that is set with of driven pulley (15.6.5), described power shaft (15.6.6) top is installed in the middle of the described case lid (15.2.1) by bearing support (15.6.7) and bearing (15.6.8), and described bearing support (15.6.7) and bearing (15.6.8) are installed on case lid (15.2.1) back side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010102491264A CN101987795B (en) | 2010-08-09 | 2010-08-09 | Special fertilizer production method and special equipment thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010102491264A CN101987795B (en) | 2010-08-09 | 2010-08-09 | Special fertilizer production method and special equipment thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101987795A CN101987795A (en) | 2011-03-23 |
CN101987795B true CN101987795B (en) | 2013-01-09 |
Family
ID=43744610
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010102491264A Active CN101987795B (en) | 2010-08-09 | 2010-08-09 | Special fertilizer production method and special equipment thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101987795B (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102219583B (en) * | 2011-04-27 | 2013-06-05 | 张冲 | Linkage device and method for composting in a large stack |
CN103478416B (en) * | 2013-08-22 | 2015-03-18 | 贵州博康生物工程有限公司 | Industrial production line of insect protein and technology for producing insect protein |
CN108263816A (en) * | 2018-01-15 | 2018-07-10 | 甘肃润牧生物工程有限责任公司 | A kind of roughage crushes and storage system |
CN108610099A (en) * | 2018-05-21 | 2018-10-02 | 贵州省遵义市道真自治县聚特农牧业有限公司 | A kind of cow dung making fertilizer process equipment |
CN111928608A (en) * | 2020-08-21 | 2020-11-13 | 安徽华星化工有限公司 | Imidacloprid secondary powder integrated drying equipment and implementation method |
CN115108854A (en) * | 2022-07-01 | 2022-09-27 | 贵州省土壤肥料研究所 | System and method for producing biofertilizer by using microorganisms and livestock and poultry manure |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5501874A (en) * | 1993-05-18 | 1996-03-26 | Mitsubishi Chemical Corporation | Method of coating granular material and apparatus therefor |
CN1316405A (en) * | 2000-04-06 | 2001-10-10 | 张兴权 | Complete set of machines for preparing compund biologic organic fertilizer from solid waste |
CN101628841A (en) * | 2009-08-19 | 2010-01-20 | 江苏亿海肥业有限公司 | Method for producing organic and inorganic compound fertilizer by utilizing duck dropping source |
CN101676243A (en) * | 2008-09-19 | 2010-03-24 | 辽宁元亨生物科技有限公司 | Production process of biological-organic-inorganic ternary compound fertilizer |
CN201756514U (en) * | 2010-08-09 | 2011-03-09 | 江阴市联业生物科技有限公司 | Special fertilizer production equipment |
-
2010
- 2010-08-09 CN CN2010102491264A patent/CN101987795B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5501874A (en) * | 1993-05-18 | 1996-03-26 | Mitsubishi Chemical Corporation | Method of coating granular material and apparatus therefor |
CN1316405A (en) * | 2000-04-06 | 2001-10-10 | 张兴权 | Complete set of machines for preparing compund biologic organic fertilizer from solid waste |
CN101676243A (en) * | 2008-09-19 | 2010-03-24 | 辽宁元亨生物科技有限公司 | Production process of biological-organic-inorganic ternary compound fertilizer |
CN101628841A (en) * | 2009-08-19 | 2010-01-20 | 江苏亿海肥业有限公司 | Method for producing organic and inorganic compound fertilizer by utilizing duck dropping source |
CN201756514U (en) * | 2010-08-09 | 2011-03-09 | 江阴市联业生物科技有限公司 | Special fertilizer production equipment |
Also Published As
Publication number | Publication date |
---|---|
CN101987795A (en) | 2011-03-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105693412B (en) | Method for preparing sheep manure organic fertilizer and processing equipment thereof | |
CN101987795B (en) | Special fertilizer production method and special equipment thereof | |
CN201801466U (en) | Production device of organic fertilizer | |
CN101429066B (en) | Method for producing fertilizer with papermaking sewage sludge | |
KR100335528B1 (en) | Organic nutritional agent for plants and the preparation method thereof | |
CN201756511U (en) | Fertilizer joint production device | |
CN105536600A (en) | Efficient fertilizer mixer for agriculture | |
CN101987800B (en) | BB fertilizer production method and special device thereof | |
CN107046961A (en) | A kind of stalk crushes the integrated apparatus of simultaneously uniform returning to the field | |
CN110317089A (en) | A kind of livestock and poultry feces and agricultural crop straw blending prepare organic fertilizer apparatus and method | |
CN104326830A (en) | Organic-inorganic compound fertilizer and preparation method thereof | |
CN102020496B (en) | Fertilizer joint production method and special device thereof | |
CN101993285B (en) | Production method of coated organic fertilizer and special equipment thereof | |
CN111807900A (en) | Preparation method of organic fertilizer | |
KR200399083Y1 (en) | an organic fertilizer and manufacturing apparatus of the same | |
CN101993284B (en) | Organic fertilizer production method and special equipment thereof | |
CN201756512U (en) | Coated organic fertilizer production device | |
CN201756513U (en) | Bulk blending BB fertilizer production device | |
CN104326773A (en) | Technology for producing biological organic fertilizer | |
CN112970371A (en) | Method for improving tobacco planting soil by returning straw stalks to field | |
CN108686551A (en) | A kind of inorganic fertilizer and organic fertilizer hybrid process system | |
CN201756514U (en) | Special fertilizer production equipment | |
JP2002248454A (en) | Treating apparatus for organic waste | |
CN110452041A (en) | A kind of production technology of microbial-bacterial fertilizer | |
CN212982826U (en) | System for producing granular organic fertilizer by utilizing biogas residue aerobic fermentation material |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: 214415 No. 6 Dazhaili Village, Jingyang Village, Zhutang Town, Jiangyin City, Jiangsu Province Patentee after: Jiangyin Pengyu Lianye Biotechnology Co., Ltd. Address before: 214415 No. 6 Dazhaili Village, Jingyang Village, Zhutang Town, Jiangyin City, Jiangsu Province Patentee before: Jiangyin Lianye Biotechology Co., Ltd. |
|
CP01 | Change in the name or title of a patent holder |