CN104860730B - Biological chelate fertilizer production technology - Google Patents
Biological chelate fertilizer production technology Download PDFInfo
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- CN104860730B CN104860730B CN201410063284.9A CN201410063284A CN104860730B CN 104860730 B CN104860730 B CN 104860730B CN 201410063284 A CN201410063284 A CN 201410063284A CN 104860730 B CN104860730 B CN 104860730B
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- alcoholization
- low temperature
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- production technology
- fertilizer production
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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
- 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
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Abstract
The invention belongs to technical field of compound fertilizer production, more particularly to a kind of production technology of biological chelate fertilizer, comprise the following steps：（1）13 parts of 36 parts of feces of livestock and poultry, 36 parts of edible fungi residue and humic acid are taken, adds the ground phosphate rock of material gross mass 1% 1.5% and the sylvite ore of material gross mass 0.5% 1.5%；Low temperature premix groove is sent into after above-mentioned material is mixed, stirred to stop 23 days, is carried out the cold fermentation of material, is obtained low temperature premix；（2）The uniform turning of low temperature premix is stopped 67 days into hot fermentation groove, obtains hot fermentation material；（3）Low temperature microbial inoculum in being added into hot fermentation material；Carry out alcoholization drying after addition, the alcoholization drying time is 23 days, obtains refining material, the water content of the alcoholization material 20% 25%；Alcoholization material obtains finished product after crushing, adding N element carrier, granulation.
Description
Technical field
The invention belongs to technical field of compound fertilizer production, more particularly to a kind of production technology of biological chelate fertilizer.
Background technology
In existing agricultural production, the specific aim of chemical fertilizer is not strong, and utilization rate is relatively low, and larger journey is polluted in agriculture face domain
Degree enters the water system of surrounding from unabsorbed fertilizer；Simultaneously during organic fertilizer use is promoted, organic fertilizer is found
Nutrient is relatively low, and organic fertilizer is directly used alone in peasant, and the yield of crop cannot improve, and directly influence the income of peasant, from
And influence the enthusiasm of peasant's manure use.Use after organic fertilizer is mixed with chemical fertilizer such as peasant, subtract although can realize
The usage amount of few chemical fertilizer, improves the quality of crop, but, planting industry is faced loss of capital in labour Gao Qi at present, so as to be not easy
Promote.
In existing market, lacking one kind enables peasant simply to use, and specific aim is stronger, and can meet that crop is complete
Face, equilibrium, the fertilizer of nutritional requirement.
The content of the invention
It is an object of the invention to provide a kind of production technology of biological chelate fertilizer, comprise the following steps：
（1）Feces of livestock and poultry 3-6 parts, edible fungi residue 3-6 parts and humic acid 1-3 parts are taken, adds material gross mass 1%-
1.5% ground phosphate rock and material gross mass 0.5%-1.5% sylvite ore；It is sent into after above-mentioned material is mixed, stirred low
Temperature premix groove stops 2-3 days, and the cold fermentation and aeration for carrying out material dehumidify；The initial temperature of cryostat, material is room temperature, just
Beginning water content is 70%-80%；After stopping 2-3 days, the temperature of material rises to 35-45 DEG C, water content 60%-65%, obtains low
Warm premix；
（2）By step（1）The obtained uniform turning of low temperature premix stops 6-7 days into hot fermentation groove, hot fermentation
The initial temperature of material is 35-45 DEG C in groove, and after stop, temperature of charge rises to 60-70 DEG C, and water content drops to 40%-45%,
Obtain hot fermentation material；
（3）To step（2）Low temperature microbial inoculum in being added in obtained hot fermentation material；Alcoholization drying is carried out after addition,
The alcoholization drying time is 2-3 days, obtains refining material, the water content 20%-25% of the alcoholization material；Refine material through powder
Finished product is obtained after broken, addition N element carrier, granulation；
The N element carrier is inorganic nitrogeneous fertilizer, preferably urea（46.4%）, calcium nitrate（11.8%）Or Diammonium phosphate (DAP)
（21.71%）In one or more, addition be material gross mass 5-10%；The dried material of alcoholization meets
NY525-2012 organic fertilizer standards.
The alcoholization is dry to be comprised the concrete steps that：It is in adding in hot fermentation material after low temperature microbial inoculum, above-mentioned material is uniform
It is distributed in several feed bins, is stacked, be aerated, refines drying process after 2-3 days and terminate.The feed bin quantity and overall life
Production capacity power matches；Aerating system and air dryer systems are disposed with the feed bin；The middle low temperature microbial inoculum is goldbeater's skin
Leukonid and/or Lactobacillus plantarum, microbial inoculum addition are the 0.1-0.8% of material gross mass.
Preferably, in step（3）Described in refine material pelletization addition humic acid, the addition of humic acid is about thing
Expect the 0.3-1% of total amount.The humic acid uses in pelletization as binding agent.
Preferably, in step（3）Described in alcoholization material pelletization terminate after alcoholization material particle surface leaching hang bacterium
Film, using air cooling, and make its drying.To be uniformly sprayed at alcoholization material particle surface, thickness is the mycoderm leaching extension mode
1-2mm；Drenching the main function of extension mycoderm is：Improve absorbability of the active and soil to fertilizer of soil.The master of the mycoderm
The species is wanted to be：Knurl bacteria agent, fixed nitrogen bacteria agent, phosphorus decomposing quasi-microorganism microbial inoculum or one kind or more in silicate microbial bacterial agent
Kind.
The advantage of the invention is that add inorganic mineral, humic acid, organic matter, microorganism in the early stage of fertilizer fermentation
Fermenting agent, therefore, during fertilizer ferments, in the presence of microorganism, under the auxiliary of humic acid, inorganic mineral substance element
Chelated by biology, form the nutrient that can be directly absorbed by crop.This middle main nutrient elements phosphorus, potassium are before fermentation
End is configured according to needed for crop and completed, and the middle also configured completion of trace element needed for crop, therefore, this way area is distinguished in original
Have fertilizer phosphorated after organic fertilizer fermentation maturation with the method for potassium, be different from after chemical fertilizer is matched plus in micro member
Method, the existing mode for the nutrient being different from fertilizer of element.The largest benefit of this technique, exactly passes through microorganism
Fermentation makes inorganic nutritive element effectively unified with organic matter, and nutrient will not occur in fertilizer with inorganic salts state again, from
And form the infringement to microorganism.For microorganism using organic matter as carrier, it is numerous to carry out the expansion of qualitative and quantitative, so as to formed with a large amount of
The fertilizer of beneficial microbe composition.By adding different microorganisms strain, the characteristic of fertilizer is set to be reflected in the acid-base value of fertilizer
On, lactic acid bacteria culturers are such as added, faintly acid fertilizer is formed by later stage fermentation can.
Under conditions of being equipped with again based on soil measurement formula, the functional form of fertilizer will be more to embody, fertilizer regulation soil acid-base
Degree, the absorbable main nutrient elements of fertilizer regulation can change soil with middle trace element, by the effect of microorganism in fertilizer
Microbial environment, the absorbable ability of crop is improved, so as to change the immunocompetence of crop.Therefore, by organic and inorganic, raw
Effective unification of thing, there is provided to the balanced comprehensive nutrient environment needed for crop, be current fertilizer technique innovation with it is integrated.
Conventional inorganic fertilizer effect release is too fast, and crops have little time to absorb, and cause fertilizer to waste；The biological chela of the present invention
The fertilizer efficiency of Hefei material constantly discharges with the growth of crops, and fertilizer efficiency utilization rate can double, the Fertilizer application in equal field
Amount（In terms of N element, P element）Reduce more than half.Other common fertilizer will not increase the content of organic matter of soil after application；
In addition, the biological chelate fertilizer of the chronic administration present invention can effectively improve the content of organic matter in soil.
Embodiment
Embodiment 1
Feces of livestock and poultry 500kg, needle mushroom dreg 400kg and humic acid 100kg are taken, adds 10kg ground phosphate rock（With P2O5
It is 33% to count content）And 5kg sylvite ore（Content is counted as 12% using KCl）；Sent after being mixed, being stirred and being turned over throwing by above-mentioned material
Enter low temperature premix groove to stop 2 days, the cold fermentation and aeration for carrying out material dehumidify；The initial temperature of cryostat, material is room temperature,
Initial water content is about 70%；After stopping 3 days, the temperature of material rises to 41 DEG C, water content 65%, obtains low temperature premix；
The uniform turning of low temperature premix is stopped 6 days into hot fermentation groove, the initial temperature of material in hot fermentation groove
For 40 DEG C, after stop, temperature of charge rises to 65 DEG C, and water content drops to 40%, obtains hot fermentation material；
Lactobacillus plantarum 500g is added into hot fermentation material；Alcoholization drying, drying time 3 are carried out after addition
My god, the water content of material is 22% after alcoholization is dried；Refine dried material to obtain after crushing, adding urea 55kg, granulation
Finished product, pelletization addition 5kg humic acid；The thick circles of the uniform sprinkling about 1mm of material particle surface are refined in granulation after terminating brown solid
Nitrogen bacterium mycoderm.Meet NY525-2012 organic fertilizer standards after testing.
Embodiment 2
Feces of livestock and poultry 600kg, flat mushroom bacteria residue 300kg and humic acid 200kg are taken, adds 16.5kg ground phosphate rock（With P2O5
It is 33% to count content）And 11kg sylvite ore（Content is counted as 12% using KCl）；After above-mentioned material is mixed, being stirred and turned over throwing
It is sent into low temperature premix groove to stop 3 days, the cold fermentation and aeration for carrying out material dehumidify；The initial temperature of cryostat, material is room
Temperature, initial water content are about 80%；After stopping 3 days, the temperature of material rises to 45 DEG C, water content 65%, obtains low temperature premix
Material；
The uniform turning of low temperature premix is stopped 6 days into hot fermentation groove, the initial temperature of material in hot fermentation groove
For 43 DEG C, after stop, temperature of charge rises to 65 DEG C, and water content drops to 45%, obtains hot fermentation material；
Leuconostoc mesenteroides 120g is added into hot fermentation material；Alcoholization drying, drying time 3 are carried out after addition
My god, the water content of material is 22% after alcoholization is dried；Refine dried material after crushing, adding calcium nitrate 110kg, granulation
Obtain finished product, pelletization addition 10kg humic acid；Granulation refines material particle surface and uniformly sprays the thick circles of about 2mm after terminating
Brown nitrogen-fixing bacteria mycoderm.Meet NY525-2012 organic fertilizer standards after testing.
The experiment effect of the field crop of embodiment 3
The soil that 20 pieces of areas are about one mu is have chosen in Nantong City Haimen City San He towns, soil regime is similar,
Random to be divided into two groups, experimental group applies the biological chelate fertilizer that the embodiment of the present invention 1 is prepared, and control group is applied commercially available general
Logical organic fertilizer；Amount of application is 700kg/ mus, remaining condition all same；Experimental result takes average per mu yield, the results showed that with it is right
Compared according to group, experimental group per mu yield improves 56kg, and rate of growth is about 15%.
Display only describes the principal character and inventive point of the present invention above.Those skilled in the art is it should be appreciated that originally
Invention is not restricted to the described embodiments.On the premise of inventive point and protection domain is not departed from, the present invention also has various changes
Change, these changes and improvements are fallen within the scope of protection of present invention.
Claims (7)
1. a kind of biological chelate fertilizer production technology, comprises the following steps：
（1）Feces of livestock and poultry 3-6 parts, edible fungi residue 3-6 parts and humic acid 1-3 parts are taken, adds material gross mass 1%-1.5%'s
The sylvite ore of ground phosphate rock and material gross mass 0.5%-1.5%；Low temperature premix is sent into after above-mentioned material is mixed, stirred
Groove stops 2-3 days, and the cold fermentation and aeration for carrying out material dehumidify；The initial temperature of cryostat, material is room temperature, initial aqueous
Measure as 70%-80%；After stopping 2-3 days, the temperature of material rises to 35-45 DEG C, water content 60%-65%, obtains low temperature premix
Material；
（2）By step（1）The obtained uniform turning of low temperature premix stops 6-7 days into hot fermentation groove, in hot fermentation groove
The initial temperature of material is 35-45 DEG C, and after stop, temperature of charge rises to 60-70 DEG C, and water content drops to 40%-45%, obtains
Hot fermentation material；
（3）To step（2）Low temperature microbial inoculum in being added in obtained hot fermentation material；Alcoholization drying is carried out after addition, it is described
It is 2-3 days to refine drying time, obtains refining material, the water content 20%-25% of the alcoholization material；The alcoholization material is through powder
Finished product is obtained after broken, addition N element carrier, granulation.
2. biological chelate fertilizer production technology as claimed in claim 1, it is characterised in that the N element carrier is urea, nitre
One or more in sour calcium or Diammonium phosphate (DAP), addition are the 5-10% of material gross mass.
3. biological chelate fertilizer production technology as claimed in claim 1, it is characterised in that the dry specific steps of the alcoholization
It is：In adding in hot fermentation material after low temperature microbial inoculum, above-mentioned material is evenly distributed in several feed bins, is stacked, exposed
Gas, refine drying process after 2-3 days and terminate.
4. biological chelate fertilizer production technology as claimed in claim 3, it is characterised in that the middle low temperature microbial inoculum is that goldbeater's skin is bright
Beading bacterium and/or Lactobacillus plantarum, microbial inoculum addition are the 0.1-0.8% of material gross mass.
5. the biological chelate fertilizer production technology as described in claim any one of 1-4, it is characterised in that in step（3）Described in
Refine material pelletization addition humic acid, the addition of humic acid is about the 0.3-1% of material total amount.
6. the biological chelate fertilizer production technology as described in claim any one of 1-4, it is characterised in that in step（3）Middle institute
State and hang mycoderm in alcoholization material particle surface leaching after alcoholization material pelletization terminates, using air cooling, and make its drying.
7. biological chelate fertilizer production technology as claimed in claim 6, it is characterised in that it is that mycoderm is equal that mycoderm is hung in the leaching
It is even to be sprayed at alcoholization material particle surface, thickness 1-2mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410063284.9A CN104860730B (en) | 2014-02-24 | 2014-02-24 | Biological chelate fertilizer production technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410063284.9A CN104860730B (en) | 2014-02-24 | 2014-02-24 | Biological chelate fertilizer production technology |
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| Publication Number | Publication Date |
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| CN104860730A CN104860730A (en) | 2015-08-26 |
| CN104860730B true CN104860730B (en) | 2018-01-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410063284.9A Expired - Fee Related CN104860730B (en) | 2014-02-24 | 2014-02-24 | Biological chelate fertilizer production technology |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110606776A (en) * | 2019-10-17 | 2019-12-24 | 郭强 | POD (peroxidase-peroxidase) simulant and process for applying POD simulant to fertilizer |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1342627A (en) * | 2001-10-30 | 2002-04-03 | 刘润发 | Organic-inorganic mixed multi-element fertilizer in chelate state |
| CN103224419A (en) * | 2013-05-05 | 2013-07-31 | 牛德山 | Production method of biological fertilizer |
| CN103588581A (en) * | 2013-11-26 | 2014-02-19 | 贵州迈丰生物科技有限责任公司 | Production process of novel cattle-dung-sourced multifunctional and efficient bioorganic fertilizer |
-
2014
- 2014-02-24 CN CN201410063284.9A patent/CN104860730B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1342627A (en) * | 2001-10-30 | 2002-04-03 | 刘润发 | Organic-inorganic mixed multi-element fertilizer in chelate state |
| CN103224419A (en) * | 2013-05-05 | 2013-07-31 | 牛德山 | Production method of biological fertilizer |
| CN103588581A (en) * | 2013-11-26 | 2014-02-19 | 贵州迈丰生物科技有限责任公司 | Production process of novel cattle-dung-sourced multifunctional and efficient bioorganic fertilizer |
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| CN104860730A (en) | 2015-08-26 |
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