CN101993284A - Organic fertilizer production method and special equipment thereof - Google Patents
Organic fertilizer production method and special equipment thereof Download PDFInfo
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- CN101993284A CN101993284A CN2010102491283A CN201010249128A CN101993284A CN 101993284 A CN101993284 A CN 101993284A CN 2010102491283 A CN2010102491283 A CN 2010102491283A CN 201010249128 A CN201010249128 A CN 201010249128A CN 101993284 A CN101993284 A CN 101993284A
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- 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
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Abstract
The invention relates to an organic fertilizer production method and special equipment thereof, which are mainly applied to the production of organic granulated fertilizers and organic-inorganic mixed granulated fertilizers. The method comprises the following steps of: mixing; stirring; fermenting in a windrow mode; turning over; maturing; drying; roughly pulverizing; screening; fine pulverizing; dispensing; pelletizing; drying; cooling; screening in stages; and finally, preparing special fertilizers, organic fertilizer agents, organic finished fertilizers, and the like. In the invention, the drying temperature of the whole production process is controlled to be 60-70 DEG C, and the drying humidity is controlled to be 30-35 percent to ensue that most microorganisms can be keep alive, thus the biological fertilizer efficiency is obvious; a special fine pulverizer is used and can be used for pulverizing when the water content of the fertilizer is 30-40 percent, thereby the production efficiency is improved by 10 times; and the fertilizer pulverizing quality is greatly improved, and pulverized fertilizer granules can be controlled to be below 1mm.
Description
(1) technical field
The present invention relates to a kind of organic class fertiliser production method and specific equipment thereof.Be mainly used in the production of organic granulated fertilizer and organic and inorganic composite grain fertilizer.
(2) background technology
Fertilizer on the market is divided into special-purpose fertilizer, common fertilizer (pulvis), common fertilizer (particle), coat fertilizer and BB fertilizer (also being Bulk Blending Fertilizer) usually.
The manufacture craft of granulated fertilizer directly affects the production efficiency and the fertilizer quality of fertilizer.Traditional fertilizer manufacture craft is normally: batching → stirring → disk pelletizing → twice hyperthermia drying (complete drying) → screening → salable product classification packing warehouse-in → unacceptable product → advance to enter next circulation after pulverizer is pulverized once more.This kind technology has the following disadvantages:
1, behind the double 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 adding inorganic additives infertile fields such as (N, P, K), the fertilizer effect is very low, serious waste of resources.
2, fertiliser granulates adopts traditional disk pelletizing technology, and granulate quality and granulation efficient are all relatively poor.
3, because granulate quality is poor, producing a large amount of coarse fodders when fertilizer screens needs further to pulverize, and production efficiency is low, and granulate quality obviously descended when returns was granulated once more simultaneously.
4, using common pulverizer, mainly is by ring mill granulation or plain grinding granulation or throwing sieve etc., and passage easily takes place during pulverizing, causes fault shut-down etc., and simultaneously, this technology dust is big, noise is big, and environmental pollution is serious.
(3) summary of the invention
The objective 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 takes place and dust is little, noise is little, the organic class fertiliser production method and the specific equipment thereof of non-environmental-pollution.
The object of the present invention is achieved like this: a kind of organic class fertiliser production method, and described method comprises following processing step:
Step 1, mixing
The raw material of preparation fertilizer is mixed by proportioning adding mixing machine, be mixed with compound, compound moisture content is controlled at 60%-65%,
The compound of step 1 preparation is added stirrer, stirs,
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 first dryer at the compound of 40%-45%, first dryer heats with first hotblast stove, the temperature of first dryer is controlled at 60 ℃-70 ℃, oven dry back water ratio is controlled at 30%-35%, first dryer utilizes the first induced draft fan air inducing, and carry out dedusting with first fly-ash separator, back up to standard discharging
Compound after will drying with Roughpulverizer is pulverized,
Carry out thickness with the compound of first sifting machine after with coarse reduction and separate, the coarse fodder that screens is got back to Roughpulverizer once more and is pulverized,
It is broken to utilize fines after slimer will screen to carry out fine powder, and pulverize back compound length and be controlled at below the 1mm,
Compound with fine powder after broken adds second mixing machine, adds some inorganic additivess by proportioning again, installs electronic scales additional on second mixing machine, carry out different proportioning weighings, mix, mixed finished product are divided into two branch lines, article one, branch line makes special-purpose fertile by check, packing and warehouse-in; Another branch line enters next step granulation,
The mixed finished product of step 10 second mixing machine are added tablets press carry out granulation,
Fertiliser granulates after the step 11 granulation is entered second drying machine drying, and second dryer heats with second hotblast stove, and bake out temperature is controlled at 60 ℃-70 ℃, oven dry back water ratio is controlled at below 10%, utilizes induced draft fan air inducing, and carries out dedusting with fly-ash separator, back up to standard discharging
Fertiliser granulates after the step 12 oven dry is entered cooler be cooled to normal temperature, cooler utilizes induced draft fan air inducing, and carries out dedusting with fly-ash separator, back up to standard discharging,
To carry out stage treatment through the cooled fertiliser granulates of step 13 with second sifting machine, the pulvis after the stage treatment is tested, is packed and puts in storage, makees organic class fertilizer pulvis and uses; Coarse grain after the stage treatment is tested, is packed and puts in storage, does organic class fertilizer coarse grain and uses; The finished product that sizing screening comes out through packing, make organic class fertilizer finished product.
The specific equipment of the organic class fertiliser production of the present invention method, comprise first mixing machine, stirrer, turnover throwing machine, transfer roller, first dryer, Roughpulverizer, first sifting machine, slimer, the batching delivery system, second mixing machine, first wrapping machine, tablets press, second dryer, cooler, second sifting machine, second wrapping machine, the 3rd wrapping machine and the 4th wrapping machine, described 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, the transfer roller outlet links to each other with the first dryer import, first dryer heats with first hotblast stove, the first dryer top is connected with first air-suction duct, the outlet of first air-suction duct links to each other with one first fly-ash separator, first fly-ash separator links to each other with one first induced draft fan, first induced draft fan links to each other with one first chimney, described 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; Import links to each other the outlet of second mixing machine with tablets press with first wrapping machine respectively; second mixing machine has electronic scales; the tablets press outlet links to each other with the second dryer import; second dryer heats with second hotblast stove; the second dryer top is connected with second air-suction duct; the outlet of second air-suction duct links to each other with one second fly-ash separator; second fly-ash separator links to each other with one second induced draft fan; second induced draft fan links to each other with one second chimney; described second dryer outlet links to each other with the cooler import; the cooler top is connected with an air-suction duct; the air-suction duct outlet links to each other with a fly-ash separator; fly-ash separator links to each other with an induced draft fan, and induced draft fan links to each other with a chimney, and the cooler outlet links to each other with the second sifting machine import; the pulvis outlet of second sifting machine links to each other with second wrapping machine; the coarse grain outlet of second sifting machine links to each other with the 3rd wrapping machine, and the finished product outlet that the sizing screening of second sifting machine comes out links to each other with the 4th wrapping machine.
The specific equipment of the organic class fertiliser production of the present invention method, 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 a 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 is evenly arranged in described power shaft periphery; On described cutter shaft, evenly be set with the multi-disc blade from top to bottom, 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 the organic class fertiliser production of the present invention method is provided with a double wedge in the middle of the outer end of described blade, all be step symmetry cloth in the both sides, outer end of blade and be provided with a plurality of double wedges, and described gear ring is a straight trough type gear ring.
The specific equipment of the organic class fertiliser production of the present invention method, 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, feed port back side outer periphery is equipped with a baffle liner.
The invention has the beneficial effects as follows:
1, the whole process of production 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 reduced noise effectively, has avoided dust pollution, has improved Working environment.
(4) description of drawings
Fig. 1 is the organic class fertiliser production of a present invention 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 a 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 a fundamental diagram one of the present invention.
Figure 13 is a 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:
First mixing machine 1; stirrer 2; bar buttress formula fermentation 3; turnover throwing machine 4; become thoroughly decomposed 5; transfer roller 6; first hotblast stove 7; first dryer 8; first air-suction duct 9; first fly-ash separator 10; first induced draft fan 11; first chimney 12; Roughpulverizer 13; first sifting machine 14; slimer 15; batching delivery system 16; second mixing machine 17; check 18; first wrapping machine 19; warehouse-in 20; tablets press 21; second hotblast stove 22; second dryer 23; second air-suction duct 24; second fly-ash separator 25; second induced draft fan 26; second chimney 27; cooler 28; air-suction duct 29; fly-ash separator 30; induced draft fan 31; chimney 32; sifting machine 33; check 34; second wrapping machine 35; warehouse-in 36; check 37; the 3rd wrapping machine 38; warehouse-in 39; check 40; the 4th wrapping machine 41; warehouse-in 42.
Support 15.1, hopper 15.2, first web member 15.3, hopper 15.4, 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
The organic class fertiliser production of the present invention method comprises following technological process:
Step 1, mixing
The raw material of preparation fertilizer is mixed by proportioning (carbon-nitrogen ratio of setting) adding mixing machine, be mixed with compound, compound moisture content is controlled 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.
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 effect of volatilization moisture fast, 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 first dryer at the compound of 40%-45%, first dryer heats with first hotblast stove, the temperature of first dryer is controlled at 60 ℃-70 ℃ (not influencing the survival temperature of bacterial classification), oven dry back water ratio is controlled at 30%-35%, first dryer utilizes the first induced draft fan air inducing, moisture content in the compound after the heating is discharged, and carry out dedusting with first fly-ash separator, discharge back up to standard.
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 first sifting machine after with coarse reduction and separate, the coarse fodder that screens is got back to Roughpulverizer once more and is pulverized.
Screening back material is still bigger, 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 with fine powder after broken adds second mixing machine, add some inorganic additivess (nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and some trace elements etc.) by proportioning again, on second mixing machine, install electronic scales additional, carry out different proportioning weighings, mix, mixed finished product are divided into two branch lines, and a branch line makes special-purpose fertile by check, packing and warehouse-in; Another branch line enters next step granulation.
The mixed finished product of step 10 second mixing machine are added tablets press carry out granulation.
Fertiliser granulates after the step 11 granulation is entered second drying machine drying, second dryer heats with second hotblast stove, bake out temperature is controlled at 60 ℃-70 ℃, oven dry back water ratio is controlled at below 10%, utilize induced draft fan air inducing, moisture content in the fertiliser granulates after the heating is discharged, and carry out dedusting, back up to standard discharging with fly-ash separator.
Fertiliser granulates after the step 12 oven dry is entered cooler be cooled to normal temperature, cooler utilizes induced draft fan air inducing, makes moisture content discharge in the cooled fertiliser granulates, and carries out dedusting with fly-ash separator, back up to standard discharging.
To carry out stage treatment through the cooled fertiliser granulates of step 13 with second sifting machine, the pulvis after the stage treatment is tested, is packed and puts in storage, makees common organic class fertilizer pulvis and uses; Coarse grain after the stage treatment is tested, is packed and puts in storage, does common organic class fertilizer coarse grain and uses; The finished product that sizing screening comes out through packing, make organic class fertilizer finished product.
Referring to Fig. 1, Fig. 1 is the organic class fertiliser production of a present invention specific equipment, comprise first mixing machine 1, stirrer 2, turnover throwing machine 4, transfer roller 6, first dryer 8, Roughpulverizer 13, first sifting machine 14, slimer 15, batching delivery system 16, second mixing machine 17, first wrapping machine 19, tablets press 21, second dryer 23, cooler 28, second sifting machine 33, second wrapping machine 35, the 3rd wrapping machine 38 and the 4th wrapping machine 41,1 outlet of described 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 first dryer, 7 heating of first dryer, 8 usefulness, first hotblast stove, first dryer, 8 tops are connected with first air-suction duct 9,9 outlets of first air-suction duct link to each other with one first fly-ash separator 10, first fly-ash separator 10 links to each other with one first induced draft fan 11, first induced draft fan 11 links to each other with one first chimney 12,8 outlets of described first dryer link to each other with Roughpulverizer 13 imports, Roughpulverizer 13 outlets link to each other with 14 imports of first sifting machine, the outlet of first sifting machine, 14 coarse fodders links to each other with Roughpulverizer 13 imports, the outlet of first sifting machine, 14 fineves links to each other with slimer 15 imports, slimer 15 outlets link to each other with 17 imports of second mixing machine, and 17 imports of second mixing machine also link to each other with batching delivery system 16; 21 imports link to each other 17 outlets of second mixing machine with tablets press with first wrapping machine 19 respectively; second mixing machine 17 has electronic scales; tablets press 21 outlets link to each other with 23 imports of second dryer; 22 heating of second dryer, 23 usefulness, second hotblast stove; second dryer, 23 tops are connected with second air-suction duct 24; 24 outlets of second air-suction duct link to each other with one second fly-ash separator 25; second fly-ash separator 25 links to each other with one second induced draft fan 26; second induced draft fan 26 links to each other with one second chimney 27; 23 outlets of described second dryer link to each other with cooler 28 imports; cooler 28 tops are connected with an air-suction duct 29; air-suction duct 29 outlets link to each other with a fly-ash separator 30; fly-ash separator 30 links to each other with an induced draft fan 31; induced draft fan 31 links to each other with a chimney 32; cooler 28 outlets link to each other with 33 imports of second sifting machine; the pulvis outlet of second sifting machine 33 links to each other with second wrapping machine 35; the coarse grain outlet of second sifting machine 33 links to each other with the 3rd wrapping machine 38; the finished product outlet that the sizing screening of second sifting machine 33 comes out links to each other with the 4th wrapping machine 41.
The present invention utilizes computer system that the whole production flow process 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.By Fig. 2, Fig. 3 and Fig. 4 as can be seen, slimer of the present invention comprises a support 15.1, and 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.By Fig. 5 and Fig. 6 as can be seen, described hopper 15.2 is cylindrical, and 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.Feed port 15.2.1.1 back side outer periphery is equipped 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 are evenly arranged in described power shaft 15.6.6 periphery.
Referring to Fig. 7～8, Fig. 7 is a hopper internal structure synoptic diagram of the present invention.Fig. 8 is the B-B sectional view of Fig. 7.By Fig. 7 and Fig. 8 as can be seen, among described four cutter shaft 15.6.10, have and all evenly be set with five blades 15.8 on two cutter shaft 15.6.10 from top to bottom, all evenly be set with four blades 15.8 from top to bottom 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 step symmetry cloth and are provided with three double wedge 15.8.2,15.8.3,15.8.4; Described gear ring 15.9 is a straight trough 15.9.1 type gear ring.
Principle of work:
Referring to Figure 12～14, Figure 12 is a fundamental diagram one of the present invention.Figure 13 is a 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, the fertilizer that arrives the hopper edge is 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 reaching 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 retaining feed back case 15.2 inside, make fertiliser granulates and dust not pass hopper and outwards go out, improved Working environment effectively.
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-purpose fertile:
So-called special-purpose fertile, be exactly nutrient uptake feature according to regional soil situation and crop, nutritive elements such as nitrogen, phosphorus, potassium and trace element are carried out scientific matching, for the special fertilizer that uses of this area crops.
Special-purpose fertilizer according to the crop growth rule with to the development and production of different element absorption amount, by 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 the special-purpose fertile compound fertilizer of various crops with suiting measures to local conditions, and at 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 Shi Hanging simultaneously, so this becomes gradually, and to solve utilization rate of fertilizer low, one of method of problem such as crop yield and downgrade.
Claims (6)
1. organic class fertiliser production method is characterized in that described method comprises following processing step:
Step 1, mixing
The raw material of preparation fertilizer is mixed by proportioning adding mixing machine, be mixed with compound, compound moisture content is controlled 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 first dryer at the compound of 40%-45%, first dryer heats with first hotblast stove, the temperature of first dryer is controlled at 60 ℃-70 ℃, oven dry back water ratio is controlled at 30%-35%, first dryer utilizes the first induced draft fan air inducing, and carry out dedusting with first fly-ash separator, back up to standard discharging
Step 7, coarse reduction
Compound after will drying with Roughpulverizer is pulverized,
Step 8, screening
Carry out thickness with the compound of first sifting machine after with coarse reduction and separate, the coarse fodder that screens is got back to Roughpulverizer once more 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 pulverize back compound length and be controlled at below the 1mm,
Step 10, batching
Compound with fine powder after broken adds second mixing machine, adds some inorganic additivess by proportioning again, installs electronic scales additional on second mixing machine, carry out different proportioning weighings, mix, mixed finished product are divided into two branch lines, article one, branch line makes special-purpose fertile by check, packing and warehouse-in; Another branch line enters next step granulation,
Step 11, granulation
The mixed finished product of step 10 second mixing machine are added tablets press carry out granulation,
Step 12, oven dry
Fertiliser granulates after the step 11 granulation is entered second drying machine drying, and second dryer heats with second hotblast stove, and bake out temperature is controlled at 60 ℃-70 ℃, oven dry back water ratio is controlled at below 10%, utilizes induced draft fan air inducing, and carries out dedusting with fly-ash separator, back up to standard discharging
Step 13, cooling
Fertiliser granulates after the step 12 oven dry is entered cooler be cooled to normal temperature, cooler utilizes induced draft fan air inducing, and carries out dedusting with fly-ash separator, back up to standard discharging,
Step 14, sizing screening
To carry out stage treatment through the cooled fertiliser granulates of step 13 with second sifting machine, the pulvis after the stage treatment is tested, is packed and puts in storage, makees organic class fertilizer pulvis and uses; Coarse grain after the stage treatment is tested, is packed and puts in storage, does organic class fertilizer coarse grain and uses; The finished product that sizing screening comes out through packing, make organic class fertilizer finished product.
2. the specific equipment of an organic according to claim 1 class fertiliser production method, it is characterized in that described equipment comprises first mixing machine (1), stirrer (2), turnover throwing machine (4), transfer roller (6), first dryer (8), Roughpulverizer (13), first sifting machine (14), slimer (15), batching delivery system (16), second mixing machine (17), first wrapping machine (19), tablets press (21), second dryer (23), cooler (28), second sifting machine (33), second wrapping machine (35), the 3rd wrapping machine (38) and the 4th wrapping machine (41), described 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 first dryer (8) import, first dryer (8) heats with first hotblast stove (7), first dryer (8) top is connected with first air-suction duct (9), first air-suction duct (9) outlet links to each other with one first fly-ash separator (10), first fly-ash separator (10) links to each other with one first induced draft fan (11), first induced draft fan (11) links to each other with one first chimney (12), described first dryer (8) outlet links to each other with Roughpulverizer (13) import, Roughpulverizer (13) outlet links to each other with first sifting machine (14) import, the outlet of first sifting machine (14) coarse fodder links to each other with Roughpulverizer (13) import, the outlet of first sifting machine (14) fines links to each other with slimer (15) import, slimer (15) outlet links to each other with second mixing machine (17) import, and second mixing machine (17) import also links to each other with batching delivery system (16); Import links to each other with tablets press (21) with first wrapping machine (19) respectively in second mixing machine (17) outlet; second mixing machine (17) has electronic scales; tablets press (21) outlet links to each other with second dryer (23) import; second dryer (23) heats with second hotblast stove (22); second dryer (23) top is connected with second air-suction duct (24); second air-suction duct (24) outlet links to each other with one second fly-ash separator (25); second fly-ash separator (25) links to each other with one second induced draft fan (26); second induced draft fan (26) links to each other with one second chimney (27); described second dryer (23) outlet links to each other with cooler (28) import; cooler (28) top is connected with an air-suction duct (29); air-suction duct (29) outlet links to each other with a fly-ash separator (30); fly-ash separator (30) links to each other with an induced draft fan (31); induced draft fan (31) links to each other with a chimney (32); cooler (28) outlet links to each other with second sifting machine (33) import; the pulvis outlet of second sifting machine (33) links to each other with second wrapping machine (35); the coarse grain outlet of second sifting machine (33) links to each other with the 3rd wrapping machine (38); the finished product outlet that the sizing screening of second sifting machine (33) comes out links to each other with the 4th wrapping machine (41).
3. the specific equipment of a kind of organic class fertiliser production method according to claim 2, 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 a 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 multi-disc blade (15.8) from top to bottom, and the dislocation of blade (15.8) in the vertical direction on two adjacent two cutter shafts (15.6.10) layout, 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).
4. the specific equipment of a kind of organic class fertiliser production method according to claim 3, 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 step symmetry cloth 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.
5. according to the specific equipment of claim 3 or 4 described a kind of organic class fertiliser 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) back side outer periphery is equipped with a baffle liner (15.2.1.2).
6. according to the specific equipment of claim 3 or 4 described a kind of organic class fertiliser production methods, 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 second web member (15.5) by bolt pair (15.7), 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.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104311180A (en) * | 2014-10-23 | 2015-01-28 | 泗县孙苏生态农业科技有限公司 | Organic fertilizer production equipment with bacterial spore separation device |
| CN105859340A (en) * | 2016-03-31 | 2016-08-17 | 登封快丰收农业发展有限公司 | Production line for bio-organic fertilizer |
| CN113582781A (en) * | 2021-08-18 | 2021-11-02 | 新疆生产建设兵团第一师农业技术推广站 | Soil remediation fertilizer and preparation method thereof |
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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. |