CN101033153A - Biochemical fertilizer and producing method thereof - Google Patents
Biochemical fertilizer and producing method thereof Download PDFInfo
- Publication number
- CN101033153A CN101033153A CNA2007100145087A CN200710014508A CN101033153A CN 101033153 A CN101033153 A CN 101033153A CN A2007100145087 A CNA2007100145087 A CN A2007100145087A CN 200710014508 A CN200710014508 A CN 200710014508A CN 101033153 A CN101033153 A CN 101033153A
- Authority
- CN
- China
- Prior art keywords
- raw material
- biochemical
- organic
- activation
- working procedure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Fertilizers (AREA)
Abstract
This invention provides a biochemical organic fertilizer containing rich active humid acid, N, P and K necessary for plants combined with biobacteriums and its production method, in which, the technical target of the fertilizer is: NPK 4-14%, organic matters 30-50%, available active bacteriums 0.2-1.0x108/g, microelements 2-6%, active humid acid 10-20% and amino acid 2-5%. The production method includes: activation and biochemical process of organic materials, granulation, drying, cooling, screening, enveloping and measuring and packaging.
Description
Technical field
The invention belongs to fertilizer field, relate to a kind of biochemical fertilizer and production method thereof.
Background technology
Soil and fertilizer are two big fundamentals of agriculture production.From the eighties in last century, China can plough the soil and use chemical fertilizer in a large number, cause that land deterioration, soil compaction, soil fertility decline, organic matter and beneficial microorganism reduce, agricultural ecological is unbalance, deterioration in quality, water resources and environment be subjected to pollution in various degree, make human health be subjected to potential and threaten.Research, development of new, non-harmful organic fertilizer are vast agricultural sciences worker's important topics.Biochemical fertilizer has become a kind of important organic fertilizer.Chinese patent 00125718.8 discloses a kind of ecological organic fertilier and preparation method thereof.This patent is a main raw material with organic waste, weathered coal, coal gangue, peat, chicken manure, adopt zymotechniques such as vinelandii, phosphate solubilizing bacteria, potassium solubilizing bacteria, make the required ecological organic fertilier of farm crop, this fertilizer contains the beneficial organism flora, the active substance of inorganic, organic substance and interpolation.This ecological organic fertilier is not thorough to organism and weathered coal conversion, and utilization ratio is low, and effective content is low, and fertilizer efficiency is short, is difficult to reach innoxious standard.Chinese patent application 03116246.0 discloses a kind of biochemical activity humic acid organic fertilizer material.This is applied for a patent disclosed biochemical activity humic acid organic fertilizer material and is made up of following component: A) contain the organism and the weathered coal of microbial inoculum, B) contain NH
4HCO
3Weathered coal, C) contain the weathered coal of KOH, D) contain (NH
2)
2The weathered coal of CO E) contains (NH
2)
2The weathered coal of CO, additive and catalyzer F) contains the inorganics of probiotics.This method complex technical process, produce discontinuous, production cost height, and have the problem that the probiotics survival rate is low and time to live is short.
Summary of the invention
The objective of the invention is to, solve fertilizer drum granulating difficulty, common weathered coal contains the difficult problem that organic 40-50% produces the high-content organic fertilizer, providing a kind of is main raw material with the weathered coal, produce be rich in activated humic acid and the required macroelement N of crop growth, P, K organise and with the method for the effective bonded biochemical fertilizer of biological bacteria.
For achieving the above object, the present invention adopts following technical scheme:
The raw material of biochemical fertilizer of the present invention is formed and weight percent is: weathered coal 70-80%, amino acid 3-8%, inorganic raw material 15-25%, microbial inoculum 0.5-1%.
Said weathered coal, its organic content 50-75%, moisture＜25%, granular size is 100 orders.
Inorganic raw material is: one or more in one or more in bicarbonate of ammonia, sodium hydroxide, wilkinite and urea, vitriolate of tartar, the monoammonium phosphate and sal epsom, zinc sulfate, ferrous sulfate, silicic acid, borax, the manganous sulfate.
Microbial inoculum is: one or more in zymophyte, 988 bacterium, vinelandii, phosphate solubilizing bacteria, the potassium solubilizing bacteria.
The technical indicator of biochemical fertilizer of the present invention is: NPK4-14%, organic 30-50%, useful active bacterium 0.2-1.0 * 10
8Individual/gram, micro-2-6%, activated humic acid 10-20%, amino acid 2-5%.
The invention provides a kind of method of producing biochemical fertilizer, processing step is as follows:
(1) the activation biochemical treatment of organic raw material: with weathered coal and bicarbonate of ammonia with weight ratio 1: 0.1-0.2 mix even after, under normal temperature, bank up a week; The 3-15% sodium hydroxide solution is sprayed in turning, and sodium hydroxide concentration is the 0.4-1.0% of weathered coal, mixes even banking up a week; Turning adds microbial inoculum again, and the microbial inoculum consumption is the 0.1-0.3% of weathered coal, banks up 2-5 days; Under 40-60 ℃, in one week of ventilating fermentation, organic raw material disposes, and is stand-by then.
(2) granulation: get organic raw material and in wilkinite in inorganic raw material and urea, vitriolate of tartar, monoammonium phosphate one or more of activation after the biochemical treatment, with weight ratio 1: 0.2-0.4 mixes, and is crushed to the 80-100 order.Above material is transported with transport tape, and transport tape top and be heated to 50-60 ℃ is on every side heated up material, and is sent into granulating working procedure.
At the granulating working procedure leading portion, spray into the atomizing ripener, material catalysis is become thoroughly decomposed, atomizing ripener consumption is the 0.05-0.1% of the organic raw material after the activation biochemical treatment.
In the granulating working procedure stage casing, spray into the atomized liquid of amino acid and trace element, after mixing, make it to take place after amino acid, the activation humic acids and inorganic raw material, micro-intersect complexing.The amino acid consumption is the 5-10% of the organic raw material after the activation biochemical treatment; Trace element is for being in the sal epsom in the inorganic raw material, zinc sulfate, ferrous sulfate, silicic acid, borax, the manganous sulfate one or more, the 2-6% of the organic raw material after its consumption activation biochemical treatment.
At the granulating working procedure back segment: the material through the granulating working procedure stage casing enters the granulating working procedure back segment automatically, adds the tackiness agent automatic granulating, the 2-5% of the organic raw material of binder dosage after for the activation biochemical treatment.
(3) oven dry: the product after the granulation, enter baker, dry to water content 12-14% baker temperature＜75 ℃.
(4) cooling: the product after will drying, send into water cooler, be cooled to normal temperature.
(5) metering packing: the conventional metering packing of the product after the processing.
(6) screening: cooled product, carry out the strictness screening, 80% of product enters coating and handles, and 20% product returns granulation after pulverizing, and is even to guarantee finished particle, improves the stability of product.
(7) coating: add 988 bacterium or other beneficial microorganism bacterium, carry out surperficial N, P, K processing, solved bacterium and combined the problem that the back survival rate is low and the time is short with inorganic salt; The employing vegetables oil is handled, and coats last layer organic plant oil at product surface, makes product have slow-release function, and its consumption is the 0.1-0.2% of material.
Biochemical fertilizer of the present invention is no chlor environmentfriendly products.(1) nutrient is complete, promptly contains the required nitrogen of plant growth, phosphorus, potassium, also contains abundant organic matter, amino acid and trace element; (2) nitrogen in the fertilizer, phosphorus, potassium 50-70% are converted into organic type, and effective constituent can be water-soluble fully, are beneficial to crop and absorb, and to give full play to fertilizer efficiency, it is obvious to use effect of increasing production on vegetables, melon and fruit, and volume increase is more than 10%; (3) compare with using mineral manure, a large amount of uses can reduce soil salinity and alkalinity, and it is strong to increase a ventilation property, keep soil from packing together, barren, improve quality of agricultural product, increase pol, improve mouthfeel; (4) improve the output of melon and fruit, vegetables, strengthen resistance against diseases, drought resistance is strong, and have the effect of remarkable promotion root system development; (5) trace element is intersected after the complexing by humic acids and amino acid, is activated at plant growth stage trace element, easily is absorbed, and is difficult for running off, and easily stores culture fertility; (6) not containing any objectionable constituent, is the green fertilizer of development novel ecological agricultural, and production cost is low, and the fertilizer height is a kind of non-harmful high-quality biochemical organic fertilizer.
This production method technology is simple, unattended automatic granulating, and the balling ratio height, production cost is low, and production continuity and operability are stronger.
Specific embodiment
Embodiment 1
With the bicarbonate of ammonia of the weathered coal of 600kg and 60kg mix even after, under normal temperature, bank up a week, 24kg10%NaOH solution is sprayed in turning, mixes even banking up a week; Turning adds 0.6kg zymophyte HM bacterium again, banks up 4 days; Under 50 ℃, ventilating fermentation fermented after 7 days then, and the organic raw material activation treatment finishes, and is stand-by.
Get activation after the biochemical treatment organic raw material 500kg and the inorganic raw material of 100kg, wherein inorganic raw material comprises urea 40kg, vitriolate of tartar 20kg, monoammonium phosphate 20kg, wilkinite 20kg after above material mixed, is crushed to 80 orders.
Above material is transported with transport tape, and transport tape top and be heated to 50 ℃ is on every side heated up material, and is sent into granulating working procedure.At the granulating working procedure leading portion, spray into 0.25kg atomizing ripener hydrogen peroxide to material, catalysis is become thoroughly decomposed; In the granulating working procedure stage casing, spray into the atomized liquid of 25kg amino acid and sal epsom 2kg, zinc sulfate 3kg, ferrous sulfate 5kg, after mixing, make it to take place after amino acid, the activation humic acids and inorganic raw material, micro-intersect complexing.At the granulating working procedure back segment: the material through the granulating working procedure stage casing enters the granulating working procedure back segment automatically, adds 10kg tackiness agent automatic granulating.Product after the granulation enters baker, and 65 ℃ of baker bake out temperatures are dried to moisture content 12%, import water cooler into, are cooled to normal temperature.Product carries out conventional metering packing.
Embodiment 2
With the bicarbonate of ammonia of the weathered coal of 600kg and 120kg mix even after, under normal temperature, bank up a week, 60kg10%NaOH solution is sprayed in turning, mixes even banking up a week; Turning adds 1.8kg zymophyte HM bacterium again, banks up 5 days; Under 60 ℃, ventilating fermentation fermented after 7 days then, and the organic raw material activation treatment finishes, and is stand-by.
Get activation after the biochemical treatment organic raw material 500kg and the inorganic raw material of 200kg, wherein inorganic raw material comprises urea 100kg, vitriolate of tartar 70kg, wilkinite 30kg after above material mixed, is crushed to 100 orders.
Above material is transported with transport tape, and transport tape top and be heated to 50 ℃ is on every side heated up material, and is sent into granulating working procedure.At the granulating working procedure leading portion, spray into 0.5kg atomizing ripener hydrogen peroxide to material, catalysis is become thoroughly decomposed; In the granulating working procedure stage casing, spray into the atomized liquid of 50kg amino acid and sal epsom 5kg, zinc sulfate 5kg, ferrous sulfate 5kg, silicic acid 5kg, borax 5kg, manganous sulfate 5kg, after mixing, make it to take place after amino acid, the activation humic acids and inorganic raw material, micro-intersect complexing.At the granulating working procedure back segment: the material through the granulating working procedure stage casing enters the granulating working procedure back segment automatically, adds 25kg tackiness agent automatic granulating.Product after the granulation enters baker, and 65 ℃ of baker bake out temperatures are dried to water content 12%, import water cooler into, are cooled to normal temperature.Product carries out conventional metering packing.
Embodiment 3
With the bicarbonate of ammonia of the weathered coal of 600kg and 90kg mix even after, under normal temperature, bank up a week, 30kg10%NaOH solution is sprayed in turning, mixes even banking up a week; Turning adds 1.2kg zymophyte HM bacterium again, banks up 4 days; Under 60 ℃, ventilating fermentation fermented after 7 days then, and the organic raw material activation treatment finishes, and is stand-by.
Get activation after the biochemical treatment organic raw material 500kg and the inorganic raw material of 150kg, wherein inorganic raw material comprises urea 40kg, monoammonium phosphate 90kg, wilkinite 20kg after above material mixed, is crushed to 80 orders, and is stand-by.
Above material is transported with transport tape, and transport tape top and be heated to 50 ℃ is on every side heated up material, and is sent into granulating working procedure.At the granulating working procedure leading portion, spray into 0.40kg atomizing ripener hydrogen peroxide to material, catalysis is become thoroughly decomposed; In the granulating working procedure stage casing, spray into the atomized liquid of 40kg amino acid and sal epsom 5kg, zinc sulfate 5kg, ferrous sulfate 5kg, borax 5kg, silicic acid 5kg, after mixing, make it to take place after amino acid, the activation humic acids and inorganic raw material, micro-intersect complexing.At the granulating working procedure back segment: the material through the granulating working procedure stage casing enters the granulating working procedure back segment automatically, adds 20kg tackiness agent automatic granulating.Product after the granulation enters baker, and 65 ℃ of baker bake out temperatures are dried to moisture content 13%, import water cooler into, are cooled to normal temperature.Product carries out conventional metering packing.
Embodiment 4
According to embodiment 1, said cooling back also has screening process in the production method.Cooled product carries out the strictness screening, and 80% of product enters baker, and 20% product returns granulation after pulverizing, and is even to guarantee finished particle, improves the stability of product.
Embodiment 5
According to embodiment 1, said cooling back also has the coating operation in the production method.Add 988 bacterium, carry out surperficial N, P, K processing, solved bacterium and combined the problem that the back survival rate is low and the time is short with inorganic salt; The employing vegetables oil is handled, and coats last layer organic plant oil at product surface, makes product have slow-release function.
Embodiment 6
According to embodiment 4, also has the coating operation in the production method behind the said screening process.Add 988 bacterium, carry out surperficial N, P, K processing, solved bacterium and combined the problem that the back survival rate is low and the time is short with inorganic salt; The employing vegetables oil is handled, and coats last layer organic plant oil at product surface, makes product have slow-release function.
Biochemical fertilizer of the present invention is no chlor environment-friendly products. (1) nutrient is complete, namely contains crop and gives birth to Long required nitrogen, phosphorus, potassium also contain abundant organic matter, amino acid and trace element; (2) in the fertilizer Nitrogen, phosphorus, potassium 50-70% be converted into organic type, active ingredient can be fully water-soluble, is beneficial to the Crop profit With, giving full play to fertilizer efficiency, vegetables, that melon and fruit is used effect of increasing production is obvious, volume increase is more than 10%; (3) Compare with using inorganic fertilizer, a large amount of uses can reduce soil salinity and alkalinity, and it is strong to increase a gas permeability, prevents Soil compaction, barren improves quality of agricultural product, increases pol, improves mouthfeel; (4) improve melon and fruit, vegetables The output of dish strengthens resistance against diseases, drought resistance is strong, and has the effect of remarkable promotion root system development; (5) Micro-by after humic acid and the complexing of amino acid intersection, be activated at plant growth stage trace element, easily Be absorbed, be difficult for running off, easily store culture fertility; (6) do not contain any harmful components, production cost is low, The fertilizer efficiency height is a kind of non-harmful high-quality biochemical organic fertilizer.
Claims (8)
1, a kind of biochemical fertilizer is characterized in that raw material is formed and weight percent is: weathered coal 70-80%, amino acid 3-8%, inorganic raw material 15-25%, microbial inoculum 0.5-1%; The technical indicator of fertilizer is: organic 30-50%, NPK4-14%, useful active bacterium 0.2-1.0 * 10
8Individual/gram, micro-2-6%, activated humic acid 10-20%, amino acid 2-5%.
2, biochemical fertilizer according to claim 1 is characterized in that the organic content 50-75% of said weathered coal, moisture＜25%, and granular size is 100 orders.
3, biochemical fertilizer according to claim 1 is characterized in that said inorganic raw material is one or more and sal epsom, zinc sulfate, ferrous sulfate, silicic acid, borax, in the manganous sulfate one or more in bicarbonate of ammonia, sodium hydroxide, wilkinite and urea, vitriolate of tartar, the monoammonium phosphate.
4, biochemical fertilizer according to claim 1 is characterized in that said microbial inoculum is one or more in zymophyte, 988 bacterium, vinelandii, phosphate solubilizing bacteria, the potassium solubilizing bacteria.
5, a kind of production method according to the described biochemical fertilizer of claim 1 is characterized in that processing step is as follows:
(1) the activation biochemical treatment of organic raw material: with weathered coal and bicarbonate of ammonia with weight ratio 1: 0.1-0.2 mix even after, under normal temperature, bank up a week; The 3-15% sodium hydroxide solution is sprayed in turning, and sodium hydroxide concentration is the 0.4-1.0% of weathered coal, mixes even banking up a week; Turning adds microbial inoculum again, and the microbial inoculum consumption is the 0.1-0.3% of weathered coal, banks up 2-5 days; Under 40-60 ℃, in one week of ventilating fermentation, organic raw material disposes, and is stand-by then.
(2) granulation: get organic raw material and in wilkinite in inorganic raw material and urea, vitriolate of tartar, monoammonium phosphate one or more of activation after the biochemical treatment, with weight ratio 1: 0.2-0.4 mixes, and is crushed to the 80-100 order.Above material is transported with transport tape, and transport tape top and be heated to 50-60 ℃ is on every side heated up material, and is sent into granulating working procedure.
At the granulating working procedure leading portion, spray into the atomizing ripener, material catalysis is become thoroughly decomposed, atomizing ripener consumption is the 0.05-0.1% of the organic raw material after the activation biochemical treatment.
In the granulating working procedure stage casing, spray into the atomized liquid of amino acid and trace element, after mixing, make it to take place after amino acid, the activation humic acids and inorganic raw material, micro-intersect complexing.The amino acid consumption is the 5-10% of the organic raw material after the activation biochemical treatment; Trace element is for being in the sal epsom in the inorganic raw material, zinc sulfate, ferrous sulfate, silicic acid, borax, the manganous sulfate one or more, the 2-6% of the organic raw material after its consumption activation biochemical treatment.
At the granulating working procedure back segment: the material through the granulating working procedure stage casing enters the granulating working procedure back segment automatically, adds the tackiness agent automatic granulating, the 2-5% of the organic raw material of binder dosage after for the activation biochemical treatment.
(3) oven dry: the product after the granulation, enter baker, dry to moisture content 12-14% baker temperature＜75 ℃.
(4) cooling: the product after will drying, send into water cooler, be cooled to normal temperature.
(5) metering packing: the conventional metering packing of the product after the processing.
6, the production method of a kind of biochemical chemical fertilizer according to claim 5 is characterized in that sieving operation in addition behind the refrigerating work procedure.
7, the production method of a kind of biochemical chemical fertilizer according to claim 5 is characterized in that also having the coating operation behind the refrigerating work procedure.
8, the production method of a kind of biochemical chemical fertilizer according to claim 6 is characterized in that sieving and also has the coating operation after the operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100145087A CN100572332C (en) | 2007-04-04 | 2007-04-04 | A kind of biochemical fertilizer and production method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100145087A CN100572332C (en) | 2007-04-04 | 2007-04-04 | A kind of biochemical fertilizer and production method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101033153A true CN101033153A (en) | 2007-09-12 |
| CN100572332C CN100572332C (en) | 2009-12-23 |
Family
ID=38729922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2007100145087A Expired - Fee Related CN100572332C (en) | 2007-04-04 | 2007-04-04 | A kind of biochemical fertilizer and production method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100572332C (en) |
Cited By (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101993298A (en) * | 2009-08-31 | 2011-03-30 | 夏荣堂 | Specific foliage fertilizer for microbial rice |
| CN102040423A (en) * | 2010-05-08 | 2011-05-04 | 王通华 | Fertility-enhancing chelating sustained-release fertilizer |
| CN102295487A (en) * | 2011-03-11 | 2011-12-28 | 山东远东国际生物化工股份有限公司 | Organic enveloped controlled-release compound fertilizer and preparation method thereof |
| CN102295478A (en) * | 2011-07-18 | 2011-12-28 | 广州市园科绿化有限公司 | Method for accelerating garden-waste compost decomposition by utilizing chemical decomposing agent |
| CN102344308A (en) * | 2011-07-02 | 2012-02-08 | 山东寿光大地绿园肥业有限公司 | Production method and device of organic-inorganic compound fertilizer |
| CN102358710A (en) * | 2011-07-26 | 2012-02-22 | 双赢集团有限公司 | Ecological fertilizer, preparation method, and application of ecological fertilizer in agricultural or forestry production |
| EP2430118A1 (en) * | 2009-05-15 | 2012-03-21 | Anthroterra Pty Ltd | Biochar complex |
| CN102391023A (en) * | 2011-08-15 | 2012-03-28 | 北京华瑞康田生物科技有限公司 | Production process for high-activity granular biologic organic fertilizer |
| CN102417426A (en) * | 2011-08-15 | 2012-04-18 | 山东金山化肥有限公司 | Production method of spraying sulfoacid resin type sustained and controlled-release fertilizer |
| CN102432390A (en) * | 2011-10-08 | 2012-05-02 | 郭现广 | Drought-resisting deep-ploughing-free nutrient leakage-prevented trace-element fertilizer |
| CN102584412A (en) * | 2011-01-10 | 2012-07-18 | 河南农飞生物科技有限公司 | Biological organic-inorganic mixed fertilizer |
| CN103755449A (en) * | 2013-12-20 | 2014-04-30 | 当涂县科辉商贸有限公司 | Efficient organic fertilizer and preparation method thereof |
| CN103755451A (en) * | 2013-12-20 | 2014-04-30 | 当涂县科辉商贸有限公司 | Microbial organic compound fertilizer and preparation method thereof |
| CN103910576A (en) * | 2014-03-28 | 2014-07-09 | 湖北省农业科学院经济作物研究所 | Organic and inorganic compound fertilizer for improving folium mori yield and quality of mulberry |
| CN103980051A (en) * | 2013-05-02 | 2014-08-13 | 付增传 | Urea formaldehyde humic acid organic fertilizer |
| CN104892130A (en) * | 2015-05-19 | 2015-09-09 | 潍坊友容实业有限公司 | A microbial fertilizer for saline-alkali land and applications thereof in plantation of vitex rotundifolia |
| CN105085111A (en) * | 2015-08-12 | 2015-11-25 | 生之道生态农业科技股份有限公司 | Biological-organic fertilizer special for corn and preparation method thereof |
| CN105152781A (en) * | 2015-09-27 | 2015-12-16 | 天津东升阳化肥股份有限公司 | Biological semi-organic fertilizer containing amino acid and making method thereof |
| CN105418329A (en) * | 2015-12-25 | 2016-03-23 | 眉山市金威特化肥有限公司 | Novel high-effective bio-composite fertilizer specially used for crops and production method thereof |
| US20170233302A1 (en) * | 2016-01-28 | 2017-08-17 | R. Umar Hasan Saputra | Process for producing coal-based fertilizer and the products produced |
| CN107141061A (en) * | 2017-05-04 | 2017-09-08 | 秦勇义 | The double micro- suit composite fertilizers of micro- microbial bacteria |
| CN107298627A (en) * | 2016-04-15 | 2017-10-27 | 孙承环 | A kind of method of use film formation at low temp technique productions ecological fertilizer |
| CN108059564A (en) * | 2017-12-25 | 2018-05-22 | 云南云叶化肥股份有限公司 | Full water-soluble fertilizer of a kind of organic and inorganic containing active microorganism and humic acid and preparation method thereof |
| CN108218639A (en) * | 2018-04-13 | 2018-06-29 | 凤台县农之梦家庭农场有限公司 | A kind of controlled release fertilizers special for flowers material and preparation method thereof |
| CN108218615A (en) * | 2017-12-25 | 2018-06-29 | 云南云叶化肥股份有限公司 | A kind of organic and inorganic humic acid fertilizer containing active microorganism and preparation method thereof |
| CN109369282A (en) * | 2018-12-27 | 2019-02-22 | 嘉施利（荆州）化肥有限公司 | A kind of organic compound fertilizer and preparation method thereof |
| CN110194702A (en) * | 2019-06-20 | 2019-09-03 | 巴州吾成农业生物科技有限公司 | A kind of fertilizer of the elimination diseases and pests of agronomic crop produced with Chinese herbal medicine |
| CN111704511A (en) * | 2020-06-22 | 2020-09-25 | 济源众德生物工程有限公司 | Preparation method of organic-inorganic compound fertilizer |
| CN113712117A (en) * | 2020-12-07 | 2021-11-30 | 广州健顺生物医药研究院有限公司 | Method for preparing organic feed from waste fruit peels |
-
2007
- 2007-04-04 CN CNB2007100145087A patent/CN100572332C/en not_active Expired - Fee Related
Cited By (32)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2430118A1 (en) * | 2009-05-15 | 2012-03-21 | Anthroterra Pty Ltd | Biochar complex |
| EP2430118A4 (en) * | 2009-05-15 | 2014-08-20 | Anthroterra Pty Ltd | Biochar complex |
| CN101993298A (en) * | 2009-08-31 | 2011-03-30 | 夏荣堂 | Specific foliage fertilizer for microbial rice |
| CN102040423A (en) * | 2010-05-08 | 2011-05-04 | 王通华 | Fertility-enhancing chelating sustained-release fertilizer |
| CN102584412A (en) * | 2011-01-10 | 2012-07-18 | 河南农飞生物科技有限公司 | Biological organic-inorganic mixed fertilizer |
| CN102295487A (en) * | 2011-03-11 | 2011-12-28 | 山东远东国际生物化工股份有限公司 | Organic enveloped controlled-release compound fertilizer and preparation method thereof |
| CN102295487B (en) * | 2011-03-11 | 2013-07-10 | 山东远东国际生物化工股份有限公司 | Organic enveloped controlled-release compound fertilizer and preparation method thereof |
| CN102344308A (en) * | 2011-07-02 | 2012-02-08 | 山东寿光大地绿园肥业有限公司 | Production method and device of organic-inorganic compound fertilizer |
| CN102295478A (en) * | 2011-07-18 | 2011-12-28 | 广州市园科绿化有限公司 | Method for accelerating garden-waste compost decomposition by utilizing chemical decomposing agent |
| CN102358710A (en) * | 2011-07-26 | 2012-02-22 | 双赢集团有限公司 | Ecological fertilizer, preparation method, and application of ecological fertilizer in agricultural or forestry production |
| CN102417426A (en) * | 2011-08-15 | 2012-04-18 | 山东金山化肥有限公司 | Production method of spraying sulfoacid resin type sustained and controlled-release fertilizer |
| CN102391023A (en) * | 2011-08-15 | 2012-03-28 | 北京华瑞康田生物科技有限公司 | Production process for high-activity granular biologic organic fertilizer |
| CN102432390A (en) * | 2011-10-08 | 2012-05-02 | 郭现广 | Drought-resisting deep-ploughing-free nutrient leakage-prevented trace-element fertilizer |
| CN103980051A (en) * | 2013-05-02 | 2014-08-13 | 付增传 | Urea formaldehyde humic acid organic fertilizer |
| CN103755449A (en) * | 2013-12-20 | 2014-04-30 | 当涂县科辉商贸有限公司 | Efficient organic fertilizer and preparation method thereof |
| CN103755451A (en) * | 2013-12-20 | 2014-04-30 | 当涂县科辉商贸有限公司 | Microbial organic compound fertilizer and preparation method thereof |
| CN103910576A (en) * | 2014-03-28 | 2014-07-09 | 湖北省农业科学院经济作物研究所 | Organic and inorganic compound fertilizer for improving folium mori yield and quality of mulberry |
| CN104892130A (en) * | 2015-05-19 | 2015-09-09 | 潍坊友容实业有限公司 | A microbial fertilizer for saline-alkali land and applications thereof in plantation of vitex rotundifolia |
| CN105085111A (en) * | 2015-08-12 | 2015-11-25 | 生之道生态农业科技股份有限公司 | Biological-organic fertilizer special for corn and preparation method thereof |
| CN105152781A (en) * | 2015-09-27 | 2015-12-16 | 天津东升阳化肥股份有限公司 | Biological semi-organic fertilizer containing amino acid and making method thereof |
| CN105418329A (en) * | 2015-12-25 | 2016-03-23 | 眉山市金威特化肥有限公司 | Novel high-effective bio-composite fertilizer specially used for crops and production method thereof |
| US20170233302A1 (en) * | 2016-01-28 | 2017-08-17 | R. Umar Hasan Saputra | Process for producing coal-based fertilizer and the products produced |
| US10683243B2 (en) * | 2016-01-28 | 2020-06-16 | R. Umar Hasan Saputra | Process for producing coal-based fertilizer and the products produced |
| CN107298627A (en) * | 2016-04-15 | 2017-10-27 | 孙承环 | A kind of method of use film formation at low temp technique productions ecological fertilizer |
| CN107141061A (en) * | 2017-05-04 | 2017-09-08 | 秦勇义 | The double micro- suit composite fertilizers of micro- microbial bacteria |
| CN108059564A (en) * | 2017-12-25 | 2018-05-22 | 云南云叶化肥股份有限公司 | Full water-soluble fertilizer of a kind of organic and inorganic containing active microorganism and humic acid and preparation method thereof |
| CN108218615A (en) * | 2017-12-25 | 2018-06-29 | 云南云叶化肥股份有限公司 | A kind of organic and inorganic humic acid fertilizer containing active microorganism and preparation method thereof |
| CN108218639A (en) * | 2018-04-13 | 2018-06-29 | 凤台县农之梦家庭农场有限公司 | A kind of controlled release fertilizers special for flowers material and preparation method thereof |
| CN109369282A (en) * | 2018-12-27 | 2019-02-22 | 嘉施利（荆州）化肥有限公司 | A kind of organic compound fertilizer and preparation method thereof |
| CN110194702A (en) * | 2019-06-20 | 2019-09-03 | 巴州吾成农业生物科技有限公司 | A kind of fertilizer of the elimination diseases and pests of agronomic crop produced with Chinese herbal medicine |
| CN111704511A (en) * | 2020-06-22 | 2020-09-25 | 济源众德生物工程有限公司 | Preparation method of organic-inorganic compound fertilizer |
| CN113712117A (en) * | 2020-12-07 | 2021-11-30 | 广州健顺生物医药研究院有限公司 | Method for preparing organic feed from waste fruit peels |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100572332C (en) | 2009-12-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100572332C (en) | A kind of biochemical fertilizer and production method thereof | |
| CN102838413B (en) | Ternary slow-release compound fertilizer and preparation method thereof | |
| CN102219604B (en) | Rice charcoal slow-release fertilizer and preparation method thereof | |
| CN103204745B (en) | Production process of ureaformaldehyde humic acid organic fertilizer | |
| CN100486941C (en) | Whole-nutrition biological flushing and spreading fertilizer and preparation method thereof | |
| CN102050644B (en) | Production method of granular bioorganic fertilizer | |
| CN102040435B (en) | Preparation method of organic slow-release fruit fertilizer | |
| CN102040407B (en) | Production method of amino acid complex microorganism fertilizer | |
| CN103044146A (en) | Complex control type long-acting controlled-release organic and inorganic biological fertilizer | |
| CN103483108B (en) | A kind of Sugarcane compound microbial fertilizer and preparation method thereof | |
| CN100364935C (en) | Organic-inorganic composite bamboo shoot coat fertilizer and its production process | |
| CN1765844A (en) | Humic acid biological fertilizer and its production method | |
| CN103964907A (en) | Silkworm excrement bio-organic fertilizer and production method thereof | |
| CN102040434B (en) | Method for producing compound microbial fertilizer by microbial inoculum packing method | |
| CN112174756A (en) | Organic-inorganic compound fertilizer and preparation method thereof | |
| CN107840760A (en) | It is a kind of to be used to adjust composite fertilizer of soil function and preparation method thereof | |
| CN105646084A (en) | Instant microelement water-soluble fertilizer capable of increasing soil organic matter content | |
| CN104058874B (en) | A kind of complex microorganism granulated fertilizer containing middle trace element and production technology thereof | |
| CN1450028A (en) | Drought-resisting biological organic fertilizer and preparation process thereof | |
| CN102040406B (en) | Method for producing compound microbial fertilizer from amino acid organic granules | |
| CN101468924A (en) | Biological organic fertilizer and production method thereof | |
| CN1445203A (en) | Quick acting composite mixed organic fertilizer with inorganic fertilizer and its producing method | |
| CN102020508A (en) | Preparation and application method of water-soluble humic acid inorganic compound fertilizer | |
| CN1344700A (en) | Efficient organic ecological fertilizer and its production process | |
| CN105884437A (en) | Biochemical organic fertilizer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20091223 Termination date: 20100404 |