CN101993284B - Organic fertilizer production method and special equipment thereof - Google Patents
Organic fertilizer production method and special equipment thereof Download PDFInfo
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- CN101993284B CN101993284B CN2010102491283A CN201010249128A CN101993284B CN 101993284 B CN101993284 B CN 101993284B CN 2010102491283 A CN2010102491283 A CN 2010102491283A CN 201010249128 A CN201010249128 A CN 201010249128A CN 101993284 B CN101993284 B CN 101993284B
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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 fertilizer 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 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 granulated fertilizer directly affects 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 again.This kind technique has the following disadvantages:
1, after double hyperthermia drying, in fertilizer, microorganism is killed totally substantially, and this kind fertilizer only rises and loosens the soil, adds organic egency, and simultaneously, by adding the infertile fields such as inorganic additives (N, P, K), the fertilizer effect is very low, serious waste of resources.
2, fertiliser granulates adopts traditional disk pelletizing technique, 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 when returns is granulated again simultaneously, granulate quality obviously descends.
4, using the Ordinary pulverization machine, is mainly grind granulation or plain grinding granulation or throw sieve etc. by ring, 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, the organic fertilizer production method of non-environmental-pollution and specific equipment thereof.
The object of the present invention is achieved like this: a kind of organic fertilizer production method, and described method comprises following processing step:
Step 1, mixing
Add mixing machine to mix by proportioning the raw material of preparation fertilizer, be mixed with compound, the compound moisture control is 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,
Bar buttress after with turnover throwing machine, step 3 being fermented turns over throwing, turns over throwing once in every 48 hours ± 5 hours, and bar buttress temperature is controlled at 65 ℃-70 ℃,
Fermented 15-20 days, compound becomes thoroughly decomposed, then passes through the stacking of 15-20 days, 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 ℃, after oven dry, moisture control is at 30%-35%, the first dryer utilizes the first induced draft fan air inducing, and carry out dedusting with the first fly-ash separator, rear discharging up to standard
Compound after drying with Roughpulverizer is pulverized,
Compound with the first sifting machine after with coarse reduction carries out thickness to be separated, and the coarse fodder that screens is again got back to Roughpulverizer and pulverized,
Utilize fines after slimer will screen to carry out fine powder broken, after pulverizing, compound length is controlled at below 1mm,
Compound after fine powder is broken adds the second mixing machine, then adds some inorganic additivess by proportioning, installs electronic scales additional on the second mixing machine, carry out different proportioning weighings, mix, mixed finished product are divided into two branch lines, article one, branch line by check, packing and warehouse-in, makes special fertilizer; Another branch line enters next step granulation,
Add tablets press to carry out granulation in step 10 the second mixed finished product of mixing machine,
Step 12, oven dry
Fertiliser granulates after the step 11 granulation is entered the second drying machine drying, and the second dryer heats with the second hotblast stove, and bake out temperature is controlled at 60 ℃-70 ℃, after oven dry, moisture control below 10%, utilizes induced draft fan air inducing, and carries out dedusting with fly-ash separator, rear discharging up to standard
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, rear discharging up to standard,
Step 14, sizing screening
To carry out stage treatment through the cooled fertiliser granulates of step 13 with the second sifting machine, the pulvis after stage treatment tests, packs and puts in storage, makees organic fertilizer pulvis and uses; Coarse grain after stage treatment tests, packs and puts in storage, does organic fertilizer coarse grain and uses; Sizing screening finished product out through packing, make organic fertilizer finished product.
the specific equipment of organic fertilizer production method of the present invention comprises 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, the first wrapping machine, tablets press, the second dryer, cooler, the second sifting machine, the second wrapping machine, the 3rd wrapping machine and the 4th wrapping machine, described the first mixing machine outlet is connected with stirrer, turnover throwing machine is arranged in the stirrer rear, transfer roller is arranged in the turnover throwing machine rear, conveyor outlet is connected 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 first air-suction duct outlet is connected with one first fly-ash separator, the first fly-ash separator is connected with one first induced draft fan, the first induced draft fan is connected with one first chimney, described the first dryer outlet is connected with the Roughpulverizer import, the Roughpulverizer outlet is connected with the first sifting machine import, the first sifting machine coarse fodder outlet is connected with the Roughpulverizer import, the first sifting machine fines outlet is connected with the slimer import, the slimer outlet is connected with the second mixing machine import, the second mixing machine import also is connected with the batching delivery system, import is connected with tablets press with the first wrapping machine respectively in the second mixing machine outlet, the second mixing machine is with electronic scales, the tablets press outlet is connected with the second dryer import, the second dryer heats with the second hotblast stove, the second dryer top is connected with the second air-suction duct, the second air-suction duct outlet is connected with one second fly-ash separator, the second fly-ash separator is connected with one second induced draft fan, the second induced draft fan is connected with one second chimney, described the second dryer outlet is connected with the cooler import, the cooler top is connected with an air-suction duct, the air-suction duct outlet is connected with a fly-ash separator, fly-ash separator is connected with an induced draft fan, induced draft fan is connected with a chimney, the cooler outlet is connected with the second sifting machine import, the pulvis outlet of the second sifting machine is connected with the second wrapping machine, the coarse grain outlet of the second sifting machine is connected with the 3rd wrapping machine, the finished product outlet out of the sizing screening of the second sifting machine, be connected with the 4th wrapping machine.
The specific equipment of organic 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 hopper, cutter head assembly is arranged 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 power shaft one on the other, the four blade axle is connected between two cutterheads of described up and down by thru-bolt, and the four blade axle to be evenly arranged in described power shaft peripheral; Evenly be set with from top to bottom the multi-disc blade on described cutter shaft, 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 described power shaft, be compounded with a gear ring at the inwall of described hopper.
The specific equipment of organic 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 organic 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 pulverize under fertilizer 30%～40% water ratio, 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 organic fertiliser production specific equipment general arrangement of the present invention.
Fig. 2 is the Facad structure schematic 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 schematic 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 in 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, the first wrapping machine 19, warehouse-in 20, tablets press 21, the second hotblast stove 22, the second dryer 23, the second air-suction duct 24, the second fly-ash separator 25, the second induced draft fan 26, the second chimney 27, cooler 28, air-suction duct 29, fly-ash separator 30, induced draft fan 31, chimney 32, sifting machine 33, check 34, the 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, 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
Organic fertilizer production method of the present invention comprises following technological process:
Step 1, mixing
Add mixing machine to mix by proportioning (carbon-nitrogen ratio of setting) raw material of preparation fertilizer, 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.
Compound after step 2 stirs is piled up the slivering buttress, carry out the fermentation of bar buttress formula.
Bar buttress after with turnover throwing machine, step 3 being fermented turns over throwing, plays pulverizing, oxygenation, promotion microbial reproduction and the effect of volatilization moisture fast, turns over throwing once in every 48 hours ± 5 hours, and bar is piled up neatly temperature and is controlled at 65 ℃-70 ℃.
Fermented 15-20 days, compound becomes thoroughly decomposed, then passes through the stacking of 15-20 days, 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), after oven dry, moisture control is at 30%-35%, the first dryer utilizes the first induced draft fan air inducing, moisture content in compound after heating is discharged, and carry out dedusting with the first fly-ash separator, rear discharging up to standard.
Compound easily lumps agglomerating in drying course, and the compound after drying with Roughpulverizer is pulverized.
Compound with the first sifting machine after with coarse reduction carries out thickness to be separated, and the coarse fodder that screens is again got back to Roughpulverizer and pulverized.
After screening, material is still larger, does not reach the requirement of granulation, utilizes fines after slimer will screen to carry out fine powder broken, and pulverizing afterwards, compound length is controlled at below 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 on the second mixing machine, carry out different proportioning weighings, mix, mixed finished product are divided into two branch lines, and a branch line makes special fertilizer by check, packing and warehouse-in; Another branch line enters next step granulation.
Add tablets press to carry out granulation in step 10 the second mixed finished product of mixing machine.
Step 12, oven dry
Fertiliser granulates after the step 11 granulation is entered the second drying machine drying, the second dryer heats with the second hotblast stove, bake out temperature is controlled at 60 ℃-70 ℃, after oven dry, moisture control is below 10%, utilize induced draft fan air inducing, moisture content in fertiliser granulates after heating is discharged, and carry out dedusting with fly-ash separator, rear discharging up to standard.
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 cooled fertiliser granulates, and carries out dedusting with fly-ash separator, rear discharging up to standard.
Step 14, sizing screening
To carry out stage treatment through the cooled fertiliser granulates of step 13 with the second sifting machine, the pulvis after stage treatment tests, packs and puts in storage, makees common organic fertilizer pulvis and uses; Coarse grain after stage treatment tests, packs and puts in storage, does common organic fertilizer coarse grain and uses; Sizing screening finished product out through packing, make organic fertilizer finished product.
referring to Fig. 1, Fig. 1 is organic fertiliser production specific equipment of the present invention, 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, the first wrapping machine 19, tablets press 21, the second dryer 23, cooler 28, the second sifting machine 33, the second wrapping machine 35, the 3rd wrapping machine 38 and the 4th wrapping machine 41, described the first mixing machine 1 outlet is connected 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 are connected with the first dryer 8 imports, first dryer 8 use the first hotblast stove 7 heating, the first dryer 8 tops are connected with the first air-suction duct 9, the first air-suction duct 9 outlets are connected with one first fly-ash separator 10, the first fly-ash separator 10 is connected with one first induced draft fan 11, the first induced draft fan 11 is connected with one first chimney 12, described the first dryer 8 outlets are connected with Roughpulverizer 13 imports, Roughpulverizer 13 outlets are connected with the first sifting machine 14 imports, the first sifting machine 14 coarse fodder outlets are connected with Roughpulverizer 13 imports, the first sifting machine 14 fines outlets are connected with slimer 15 imports, slimer 15 outlets are connected with the second mixing machine 17 imports, the second mixing machine 17 imports also are connected with batching delivery system 16, 21 imports are connected with tablets press with the first wrapping machine 19 respectively in the second mixing machine 17 outlets, the second mixing machine 17 is with electronic scales, tablets press 21 outlets are connected with the second dryer 23 imports, second dryer 23 use the second hotblast stove 22 heating, the second dryer 23 tops are connected with the second air-suction duct 24, the second air-suction duct 24 outlets are connected with one second fly-ash separator 25, the second fly-ash separator 25 is connected with one second induced draft fan 26, the second induced draft fan 26 is connected with one second chimney 27, described the second dryer 23 outlets are connected with cooler 28 imports, cooler 28 tops are connected with an air-suction duct 29, air-suction duct 29 outlets are connected with a fly-ash separator 30, fly-ash separator 30 is connected with an induced draft fan 31, induced draft fan 31 is connected with a chimney 32, cooler 28 outlets are connected with the second sifting machine 33 imports, the pulvis outlet of the second sifting machine 33 is connected with the second wrapping machine 35, the coarse grain outlet of the second sifting machine 33 is connected with the 3rd wrapping machine 38, the finished product outlet out of the sizing screening of the second sifting machine 33, be connected with the 4th wrapping machine 41.
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 schematic 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 by Fig. 2, Fig. 3 and Fig. 4, 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.Can be found out by Fig. 5 and Fig. 6, 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 in Fig. 2 can enter in 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 arranged on web member 15.5 by bolt pair 15.7 (quadruplet), electrical machine belt pulley 15.6.4 is arranged on motor 15.6.2 output terminal, transmission belt 15.6.3 is sleeved on electrical machine belt pulley 15.6.4 and driven pulley 15.6.5, driven pulley 15.6.5 is arranged on 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 arranged in the middle of 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 hopper 15.2, cutter head assembly is arranged on the interior power shaft 15.6.6 of 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 power shaft 15.6.6 one on the other, four blade axle 15.6.10 is connected between 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 hopper internal structure schematic 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, in 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 another two cutter shaft 15.6.10, and the 15.8 in the vertical direction dislocation of the blade on two adjacent two cutter shaft 15.6.10 are 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 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, after the position of Fig. 9 started power system 15.6 runnings, totally 18 blades 15.8 on four cutter shaft 15.6.10 were thrown away at once when blade.
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 case lid 15.2.1 by hopper 15.2 after fertilizer 15.10 enters hopper 15.4 enters in hopper 15.2, 18 blades 15.8 in hopper under the driving of power system 15.6 in hopper high speed rotating, with the continuous cutting and grinding of fertilizer 15.10 that enter in 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 at arrival 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 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 after 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):
In organism, the total content of carbon is called carbon-nitrogen ratio with the ratio of the total content of nitrogen.
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 is 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, therefore this becomes gradually that to solve utilization rate of fertilizer low, one of method of the problem such as crop yield and Quality Down.
Claims (6)
1. organic fertilizer production method is characterized in that described method comprises following processing step:
Step 1, mixing
Add mixing machine to mix by proportioning the raw material of preparation fertilizer, 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
Bar buttress after with turnover throwing machine, step 3 being fermented turns over throwing, turns over throwing once in every 48 hours ± 5 hours, and bar buttress temperature is controlled at 65 ℃-70 ℃,
Step 5, become thoroughly decomposed
Fermented 15-20 days, compound becomes thoroughly decomposed, then passes through the stacking of 15-20 days, 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 ℃, after oven dry, moisture control is at 30%-35%, the first dryer utilizes the first induced draft fan air inducing, and carry out dedusting with the first fly-ash separator, rear discharging up to standard
Step 7, coarse reduction
Compound after drying with Roughpulverizer is pulverized,
Step 8, screening
Compound with the first sifting machine after with coarse reduction carries out thickness to be separated, and the coarse fodder that screens is again got back to Roughpulverizer and pulverized,
Step 9, fine powder are broken
Utilize fines after slimer will screen to carry out fine powder broken, after pulverizing, compound length is controlled at below 1mm,
Step 10, batching
Compound after fine powder is broken adds the second mixing machine, then adds some inorganic additivess by proportioning, installs electronic scales additional on the second mixing machine, carry out different proportioning weighings, mix, mixed finished product are divided into two branch lines, article one, branch line by check, packing and warehouse-in, makes special fertilizer; Another branch line enters next step granulation,
Step 11, granulation
Add tablets press to carry out granulation in step 10 the second mixed finished product of mixing machine,
Step 12, oven dry
Fertiliser granulates after the step 11 granulation is entered the second drying machine drying, and the second dryer heats with the second hotblast stove, and bake out temperature is controlled at 60 ℃-70 ℃, after oven dry, moisture control below 10%, utilizes induced draft fan air inducing, and carries out dedusting with fly-ash separator, rear discharging up to standard
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, rear discharging up to standard,
Step 14, sizing screening
To carry out stage treatment through the cooled fertiliser granulates of step 13 with the second sifting machine, the pulvis after stage treatment tests, packs and puts in storage, makees organic fertilizer pulvis and uses; Coarse grain after stage treatment tests, packs and puts in storage, does organic fertilizer coarse grain and uses; Sizing screening finished product out through packing, make organic fertilizer finished product.
2. the specific equipment of organic fertilizer production method as claimed in claim 1, is characterized in that described equipment 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), the first wrapping machine (19), tablets press (21), the second dryer (23), cooler (28), the second sifting machine (33), the second wrapping machine (35), the 3rd wrapping machine (38) and the 4th wrapping machine (41), described the first mixing machine (1) outlet is connected 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 is connected 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 is connected with one first fly-ash separator (10), the first fly-ash separator (10) is connected with one first induced draft fan (11), the first induced draft fan (11) is connected with one first chimney (12), described the first dryer (8) outlet is connected with Roughpulverizer (13) import, Roughpulverizer (13) outlet is connected with the first sifting machine (14) import, the outlet of the first sifting machine (14) coarse fodder is connected with Roughpulverizer (13) import, the outlet of the first sifting machine (14) fines is connected with slimer (15) import, slimer (15) outlet is connected with the second mixing machine (17) import, the second mixing machine (17) import also is connected with batching delivery system (16), import is connected with tablets press (21) with the first wrapping machine (19) respectively in the second mixing machine (17) outlet, the second mixing machine (17) is with electronic scales, tablets press (21) outlet is connected with the second dryer (23) import, the second dryer (23) heats with the second hotblast stove (22), the second dryer (23) top is connected with the second air-suction duct (24), the second air-suction duct (24) outlet is connected with one second fly-ash separator (25), the second fly-ash separator (25) is connected with one second induced draft fan (26), the second induced draft fan (26) is connected with one second chimney (27), described the second dryer (23) outlet is connected with cooler (28) import, cooler (28) top is connected with an air-suction duct (29), air-suction duct (29) outlet is connected with one the 4th fly-ash separator (30), the 4th fly-ash separator (30) is connected with an induced draft fan (31), induced draft fan (31) is connected with a chimney (32), cooler (28) outlet is connected with the second sifting machine (33) import, the pulvis outlet of the second sifting machine (33) is connected with the second wrapping machine (35), the coarse grain outlet of the second sifting machine (33) is connected with the 3rd wrapping machine (38), the finished product outlet out of the sizing screening of the second sifting machine (33), be connected with the 4th wrapping machine (41).
3. the specific equipment of a kind of organic fertilizer production method according to claim 2,
It is characterized in thatDescribed 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 hopper (15.2), cutter head assembly is arranged 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 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, evenly be set with from top to bottom multi-disc blade (15.8) on described cutter shaft (15.6.10), 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 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 fertilizer production method according to claim 3, it is characterized in that being provided with a double wedge (15.8.1) in the middle of the outer end of described blade (15.8), 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.
5. the specific equipment of according to claim 3 or 4 described a kind of organic 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 on one side a feed port (15.2.1.1), and feed port (15.2.1.1) periphery, the back side is provided with a baffle liner (15.2.1.2).
6. the specific equipment of a kind of organic fertilizer production method according to claim 5, 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 arranged on the second web member (15.5) by bolt pair (15.7), the second web member (15.5) is arranged on support (15.1), electrical machine belt pulley (15.6.4) is arranged on motor (15.6.2) output terminal, transmission belt (15.6.3) is sleeved on electrical machine belt pulley (15.6.4) and driven pulley (15.6.5), driven pulley (15.6.5) is arranged on 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 arranged in the middle of 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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| CN2010102491283A CN101993284B (en) | 2010-08-09 | 2010-08-09 | Organic fertilizer production method and special equipment thereof |
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| CN104311180B (en) * | 2014-10-23 | 2017-06-16 | 泗县孙苏生态农业科技有限公司 | A kind of organic fertilizer production equipment with bacterium bag separator |
| 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 |
| CN113582781B (en) * | 2021-08-18 | 2022-09-06 | 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 |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1236765A (en) * | 1999-04-13 | 1999-12-01 | 中国农业工程研究设计院 | Drying-granulating integrated process for preparing granular compound organic fertilizer and its complete set of apparatuses |
| CN101462899A (en) * | 2008-11-14 | 2009-06-24 | 林晓山 | Technique for producing humic acid organic compound fertilizer from sugar refinery waste slag and wastewater |
| CN201801466U (en) * | 2010-08-09 | 2011-04-20 | 江阴市联业生物科技有限公司 | Production device of organic fertilizer |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JPH01172293A (en) * | 1987-12-25 | 1989-07-07 | Mitsubishi Kasei Corp | Production of bulk blend fertilizer |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1236765A (en) * | 1999-04-13 | 1999-12-01 | 中国农业工程研究设计院 | Drying-granulating integrated process for preparing granular compound organic fertilizer and its complete set of apparatuses |
| CN101462899A (en) * | 2008-11-14 | 2009-06-24 | 林晓山 | Technique for producing humic acid organic compound fertilizer from sugar refinery waste slag and wastewater |
| CN201801466U (en) * | 2010-08-09 | 2011-04-20 | 江阴市联业生物科技有限公司 | Production device of organic fertilizer |
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| Title |
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| JP平1-172293A 1989.07.07 |
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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. |