CN111269062A - Micro-amino acid compound fertilizer and preparation process thereof - Google Patents
Micro-amino acid compound fertilizer and preparation process thereof Download PDFInfo
- Publication number
- CN111269062A CN111269062A CN202010250051.5A CN202010250051A CN111269062A CN 111269062 A CN111269062 A CN 111269062A CN 202010250051 A CN202010250051 A CN 202010250051A CN 111269062 A CN111269062 A CN 111269062A
- Authority
- CN
- China
- Prior art keywords
- parts
- amino acid
- micro
- compound fertilizer
- acid compound
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C11/00—Other nitrogenous fertilisers
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
-
- 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
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Pest Control & Pesticides (AREA)
- Fertilizers (AREA)
Abstract
The invention discloses a micro-amino acid compound fertilizer and a preparation process thereof, wherein 100-150 parts of plant straws are crushed at 200-300 r/min by a crushing roller of a crusher, crushed straw scraps are screened to remove mud and impurities in the straw scraps, then the straw scraps are placed into a fermentation kettle, 20-40 parts of water is added, the fermentation kettle is heated to 200-300 ℃, the straw scraps are continuously steamed at 200-300 ℃ for 30-50 min, the water is evaporated to dryness to obtain the straw scraps with the water content of 60-80%, and the straw scraps with the water content of 60-80% are placed into the fermentation kettle. The micro-amino acid compound fertilizer and the preparation process thereof have the advantages that the micro-amino acid compound fertilizer has good antiviral property for crops by matching pinene, matrine and nicotine, can stimulate and adjust the rapid growth of the crops, promote the crops to grow robustly and promote the absorption of nutrient substances, avoid the forced damage of viruses to the crops and effectively improve the planting yield of the crops.
Description
Technical Field
The invention relates to the technical field of organic fertilizers, in particular to a micro-amino acid compound fertilizer and a preparation process thereof.
Background
Organic fertilizer, mainly from plants and/or animals, is applied to the soil to provide plant nutrition as a carbon-containing material with the main function. Is prepared from biological substances, animal and plant wastes and plant residues, eliminates toxic and harmful substances in the biological substances, and is rich in a large amount of beneficial substances, including: various organic acids, peptides and rich nutrient elements including nitrogen, phosphorus and potassium. The fertilizer not only can provide comprehensive nutrition for crops, but also has long fertilizer efficiency, can increase and update soil organic matters, promote microbial propagation, improve the physical and chemical properties and biological activity of soil, and is a main nutrient for green food production.
The amino acid fertilizer, a fertilizer containing amino acid substances, has no national standard yet. Amino acid exists in the fertilizer as the minimum molecule of the protein, and has the characteristic of being easily absorbed by crops; also has the functions of improving disease resistance of the fertilization objects and improving the quality of the fertilization crops. Supplementing essential amino acids, stimulating and regulating plant growth, promoting plant growth, and promoting nutrient absorption. The metabolism function of the plant is enhanced, the photosynthesis is improved, the development of the root system of the plant is promoted, and the growth and the propagation of the plant are accelerated.
The existing amino acid fertilizer can stimulate and adjust the fast growth of crops, promote the crops to grow strongly and promote the absorption of nutrient substances, but cannot effectively achieve the antiviral effect on the crops, and the traditional antiviral method has little harm to the soil and human bodies by spraying pesticides, so that the invention of the micro amino acid compound fertilizer is urgently needed.
Disclosure of Invention
Technical problem to be solved
Aiming at the defects of the prior art, the invention provides the micro-amino acid compound fertilizer and the preparation process thereof, which have the advantages of crop virus resistance, no harm to the land and the human body and the like, and solve the problem that the traditional virus resistance is that pesticide spraying causes little harm to the land and the human body.
(II) technical scheme
In order to achieve the purpose of resisting viruses of crops, the invention provides the following technical scheme: a micro-amino acid compound fertilizer comprises the following raw materials in parts by weight: 100-150 parts of plant straw, 20-50 parts of amino acid solution, 5-10 parts of zymocyte, 20-40 parts of water, 10-30 parts of pinene, 5-10 parts of matrine and 3-5 parts of nicotine.
Preferably, the plant straw is one or more of soybean, corn, peanut, tomato and the like.
Preferably, the amino acid solution is composed of 2-3 parts of indoleacetic acid solution, 1-3 parts of indolepropionic acid solution, 5-7 parts of naphthylacetic acid solution, 6-9 parts of methyl naphthylacetate and 4-8 parts of gibberellin solution, 2-3 parts of indoleacetic acid solution, 1-3 parts of indolepropionic acid solution, 5-7 parts of naphthylacetic acid solution, 6-9 parts of methyl naphthylacetate and 4-8 parts of gibberellin solution are placed into a mixing device to be mixed for 10-20 min at the temperature of 60-70 ℃, and finally the amino acid solution is obtained after standing for 5-10 min.
Preferably, the fermentation bacteria comprise 5-10 parts of bacillus subtilis, 1-3 parts of cellulase, 2-4 parts of potassium perphosphate and 10-20 parts of distilled water, and the bacillus subtilis 5-10 parts of cellulase, 1-3 parts of cellulase, 2-4 parts of potassium perphosphate and 10-20 parts of distilled water are sequentially placed into a fermentation kettle to be fermented for 3-5 hours at the temperature of 30-35 ℃.
Preferably, the pinene is obtained by fractionating turpentine or white camphor oil serving as a raw material.
Preferably, the matrine is prepared by extracting dried root, plant and fruit of Sophora flavescens ait of Leguminosae with organic solvent such as ethanol.
Preferably, the nicotine is obtained by extracting plant of Solanaceae (Solanum) with organic solvent such as ethanol.
The invention aims to solve another technical problem of providing a process for preparing a micro-amino acid compound fertilizer, which comprises the following steps:
s1 preparation of raw materials
100-150 parts of plant straws are crushed at a speed of 200-300 r/min by a crushing roller of a crusher, crushed straw scraps are screened to remove soil and impurities in the straw scraps, then the straw scraps are placed into a fermentation kettle, 20-40 parts of water is added, the fermentation kettle is heated to 200-300 ℃, the straw scraps are continuously steamed at a high temperature of 200-300 ℃ for 30-50 min, and the water is evaporated to obtain the straw scraps with a water content of 60-80%.
S2 preparation of fermentation
Putting straw scraps with the water content of 60-80% into a fermentation kettle, setting the temperature in the fermentation kettle to be 30-35 ℃, pouring 20-50 parts of amino acid solution into the fermentation kettle, continuously fermenting at the temperature of 25-30 ℃ for 10-20 hours, completing fermentation, raising the temperature of the fermentation kettle to 90-120 ℃, evaporating water in the fermentation kettle for 30-40 min, and evaporating the water content of a fermented product to 40-60% to obtain a rough micro amino acid compound fertilizer.
S3 disease-resistant treatment
Putting the obtained rough micro-amino acid compound fertilizer into a drying furnace, sequentially putting 10-30 parts of pinene, 5-10 parts of matrine and 3-5 parts of nicotine into the drying furnace, stirring the stirring shaft at 500-1000 r/min for 30-60 min to achieve the purpose of fully halving, finally heating the drying device to 100-200 ℃, stirring and drying for 40-50 min to obtain the micro-amino acid compound fertilizer.
(III) advantageous effects
Compared with the prior art, the invention provides a micro-amino acid compound fertilizer and a preparation process thereof, and the micro-amino acid compound fertilizer has the following beneficial effects:
1. the micro-amino acid compound fertilizer and the preparation process thereof have the advantages that the micro-amino acid compound fertilizer has good antiviral property for crops by matching pinene, matrine and nicotine, can stimulate and adjust the rapid growth of the crops, promote the growth of the crops to be robust, promote the absorption of nutrient substances, avoid the crop from being forced by virus, and effectively improve the planting yield of the crops.
2. According to the micro-amino acid compound fertilizer and the preparation process thereof, pinene, matrine and nicotine extracted from plants can be well degraded, the problem that pesticide residues are eaten by human bodies to cause discomfort is avoided, and the micro-amino acid compound fertilizer can be further conveniently absorbed by crops by adding the amino acid solution, so that the aims of stimulating and adjusting the rapid growth of the crops, promoting the robust growth of the crops and promoting the absorption of nutrient substances are better achieved.
3. According to the micro-amino acid compound fertilizer and the preparation process thereof, the micro-amino acid compound fertilizer is obtained through the raw material straws, the cost of the micro-amino acid compound fertilizer can be effectively saved, the problem that the traditional straw burning pollutes the atmospheric environment can be effectively solved, the purpose of energy saving is achieved to a certain extent, and the characteristic of convenience in raw material selection is achieved.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The first embodiment is as follows:
a micro-amino acid compound fertilizer comprises the following raw materials in parts by weight: 100 parts of plant straw, 20 parts of amino acid solution, 5 parts of zymocyte, 20 parts of water, 10 parts of pinene, 5 parts of matrine and 3 parts of nicotine.
Wherein: the plant straw is one or more of soybean, corn, peanut, tomato, etc.
And the amino acid solution consists of 2 parts of indoleacetic acid solution, 1 part of indolepropionic acid solution, 5 parts of naphthylacetic acid solution, 6 parts of methyl naphthylacetate and 4 parts of gibberellin solution, and the 2 parts of indoleacetic acid solution, 1 part of indolepropionic acid solution, 5 parts of naphthylacetic acid solution, 6 parts of methyl naphthylacetate and 4 parts of gibberellin solution are put into a mixing device to be mixed for 10min at the temperature of 60 ℃, and finally, the mixture is kept stand for 5min to obtain the amino acid solution.
The fermentation bacteria comprise 5 parts of bacillus subtilis, 1 part of cellulase, 2 parts of potassium perphosphate and 10 parts of distilled water, and the bacillus subtilis, the cellulase, the potassium perphosphate and the distilled water are sequentially put into a fermentation kettle to be fermented for 3 hours at the temperature of 30 ℃.
The pinene is obtained by fractionating turpentine oil or white camphor oil serving as a raw material.
The matrine is prepared from dried root, plant and fruit of Sophora flavescens ait of Leguminosae by extracting with organic solvent such as ethanol.
Nicotine is prepared by extracting plant (Solanum) of Solanaceae with organic solvent such as ethanol.
A process for preparing a micro-amino acid compound fertilizer comprises the following steps:
s1 preparation of raw materials
100 parts of plant straws are crushed at 200r/min by a crushing roller of a crusher, crushed straw scraps are screened to remove soil and impurities in the straw scraps, then the straw scraps are put into a fermentation kettle, 20 parts of water is added, the fermentation kettle is heated to 200 ℃, the continuous high temperature of 200 ℃ is steamed and boiled for 30min, and the water is evaporated to dryness to obtain the straw scraps with the water content of 60%.
S2 preparation of fermentation
Putting the straw scraps with the water content of 60% into a fermentation kettle, setting the temperature in the fermentation kettle to be 30 ℃, pouring 20 parts of amino acid solution into the fermentation kettle, continuously fermenting at the temperature of 25 ℃ for 10 hours, raising the temperature of the fermentation kettle to 90 ℃ after fermentation is finished, evaporating for 30min to evaporate water in the fermentation kettle, and evaporating the water content of a fermented product to 40% to obtain the rough micro amino acid compound fertilizer.
S3 disease-resistant treatment
And putting the obtained crude micro-amino acid compound fertilizer into a drying furnace, sequentially putting 10 parts of pinene, 5 parts of matrine and 3 parts of nicotine into the drying furnace, stirring the stirring shaft for 30min at a speed of 500r/min to achieve the purpose of fully reducing half, finally heating the dryer to 100 ℃, stirring and drying for 40min to obtain the micro-amino acid compound fertilizer.
Example two:
a micro-amino acid compound fertilizer comprises the following raw materials in parts by weight: 120 parts of plant straws, 30 parts of amino acid solution, 7 parts of zymocyte, 25 parts of water, 15 parts of pinene, 6 parts of matrine and 3.5 parts of nicotine.
Wherein: the plant straw is one or more of soybean, corn, peanut, tomato, etc.
The amino acid solution is composed of 2.5 parts of indoleacetic acid solution, 2.5 parts of indolepropionic acid solution, 6 parts of naphthylacetic acid solution, 7 parts of naphthylacetic acid methyl ester and 6 parts of gibberellin solution, 2.5 parts of indoleacetic acid solution, 1.5 parts of indolepropionic acid solution, 5.5 parts of naphthylacetic acid solution, 7 parts of naphthylacetic acid methyl ester and 6 parts of gibberellin solution are placed into a mixing device to be mixed for 15min at 65 ℃, and finally the amino acid solution is obtained after the mixture is kept stand for 7 min.
The fermentation bacteria comprise Bacillus subtilis 6, cellulase 2, potassium perphosphate 3, and distilled water 15, and the Bacillus subtilis 7, cellulase 1.5, potassium perphosphate 2.5, and distilled water 15 are sequentially placed in a fermentation kettle and fermented at 32 deg.C for 3.5 h.
The pinene is obtained by fractionating turpentine oil or white camphor oil serving as a raw material.
The matrine is prepared from dried root, plant and fruit of Sophora flavescens ait of Leguminosae by extracting with organic solvent such as ethanol.
Nicotine is prepared by extracting plant (Solanum) of Solanaceae with organic solvent such as ethanol.
A process for preparing a micro-amino acid compound fertilizer comprises the following steps:
s1 preparation of raw materials
120 parts of plant straws are crushed at 240r/min by a crushing roller of a crusher, crushed straw scraps are screened to remove soil and impurities in the straw scraps, then the straw scraps are put into a fermentation kettle, 25 parts of water is added, the fermentation kettle is heated to 240 ℃, the continuous high temperature of 240 ℃ is steamed and boiled for 35min, and the water is evaporated to dryness to obtain the straw scraps with the water content of 65%.
S2 preparation of fermentation
Putting the straw scraps with the water content of 65% into a fermentation kettle, setting the temperature in the fermentation kettle to be 32 ℃, pouring 30 parts of amino acid solution into the fermentation kettle, continuously fermenting for 15 hours at the temperature of 27 ℃, raising the temperature of the fermentation kettle to 100 ℃ after fermentation is completed, evaporating for 32min to evaporate water in the fermentation kettle, evaporating the water content of a fermented product to 45% to obtain the rough micro amino acid compound fertilizer.
S3 disease-resistant treatment
Putting the obtained crude micro-amino acid compound fertilizer into a drying furnace, sequentially putting 15 parts of pinene, 6 parts of matrine and 3.5 parts of nicotine into the drying furnace, stirring the stirring shaft for 40min at 700r/min to achieve the purpose of fully halving, finally heating the dryer to 130 ℃, stirring and drying for 43min to obtain the micro-amino acid compound fertilizer.
Example three:
a micro-amino acid compound fertilizer comprises the following raw materials in parts by weight: 140 parts of plant straw, 40 parts of amino acid solution, 8 parts of zymocyte, 30 parts of water, 20 parts of pinene, 8 parts of matrine and 4 parts of nicotine.
Wherein: the plant straw is one or more of soybean, corn, peanut, tomato, etc.
The amino acid solution is composed of 2.7 parts of indoleacetic acid solution, 2.7 parts of indolepropionic acid solution, 6.5 parts of naphthylacetic acid solution, 8 parts of methyl naphthylacetate and 7 parts of gibberellin solution, 2.7 parts of indolepropionic acid solution, 6 parts of naphthylacetic acid solution, 8 parts of methyl naphthylacetate and 7 parts of gibberellin solution are placed into a mixing device to be mixed for 17min at 67 ℃, and finally the amino acid solution is obtained after standing for 8 min.
The fermentation bacteria comprise bacillus subtilis 8, cellulase 2.5, potassium perphosphate 3.5 and distilled water 17, and the bacillus subtilis 8, the cellulase 2, the potassium perphosphate 3 and the distilled water 17 are sequentially put into a fermentation kettle to be fermented for 4 hours at the temperature of 34 ℃.
The pinene is obtained by fractionating turpentine oil or white camphor oil serving as a raw material.
The matrine is prepared from dried root, plant and fruit of Sophora flavescens ait of Leguminosae by extracting with organic solvent such as ethanol.
Nicotine is prepared by extracting plant (Solanum) of Solanaceae with organic solvent such as ethanol.
A process for preparing a micro-amino acid compound fertilizer comprises the following steps:
s1 preparation of raw materials
And (2) stirring 140 parts of plant straws at 250r/min by using a crushing roller of a crusher, screening the crushed straw scraps, removing soil and impurities in the straw scraps, then putting the straw scraps into a fermentation kettle, adding 30 parts of water, heating the fermentation kettle to 250 ℃, continuously steaming at 260 ℃ for 40min, and evaporating the water to dryness to obtain the straw scraps with the water content of 70%.
S2 preparation of fermentation
Putting the straw scraps with the water content of 70% into a fermentation kettle, setting the temperature in the fermentation kettle to be 34 ℃, pouring 40 parts of amino acid solution into the fermentation kettle, continuously fermenting at the temperature of 28 ℃ for 18 hours, raising the temperature of the fermentation kettle to 110 ℃ after fermentation is finished, evaporating for 35min to evaporate water in the fermentation kettle, and evaporating the water content of a fermented product to 55% to obtain the rough micro amino acid compound fertilizer.
S3 disease-resistant treatment
And putting the obtained crude micro-amino acid compound fertilizer into a drying furnace, sequentially putting 20 parts of pinene, 8 parts of matrine and 4 parts of nicotine into the drying furnace, stirring the stirring shaft for 50min at the speed of 800r/min to achieve the purpose of fully reducing the half, finally heating the dryer to 150 ℃, stirring and drying for 44min to obtain the micro-amino acid compound fertilizer.
Experimental example four:
a micro-amino acid compound fertilizer comprises the following raw materials in parts by weight: 50 parts of plant straw, 50 parts of amino acid solution, 10 parts of zymocyte, 40 parts of water, 30 parts of pinene, 10 parts of matrine and 5 parts of nicotine.
Wherein: the plant straw is one or more of soybean, corn, peanut, tomato, etc.
And the amino acid solution is composed of 3 parts of indoleacetic acid solution, 3 parts of indolepropionic acid solution, 7 parts of naphthylacetic acid solution, 9 parts of methyl naphthylacetate and 8 parts of gibberellin solution, and the 3 parts of indoleacetic acid solution, 3 parts of indolepropionic acid solution, 7 parts of naphthylacetic acid solution, 9 parts of methyl naphthylacetate and 8 parts of gibberellin solution are placed into a mixing device to be mixed for 20min at 70 ℃, and finally the mixture is kept stand for 10min to obtain the amino acid solution.
The fermentation bacteria comprise 10 parts of bacillus subtilis, 3 parts of cellulase, 4 parts of potassium perphosphate and 20 parts of distilled water, and the bacillus subtilis, the cellulase, the potassium perphosphate and the distilled water are sequentially put into a fermentation kettle to be fermented for 5 hours at the temperature of 35 ℃.
The pinene is obtained by fractionating turpentine oil or white camphor oil serving as a raw material.
The matrine is prepared from dried root, plant and fruit of Sophora flavescens ait of Leguminosae by extracting with organic solvent such as ethanol.
Nicotine is prepared by extracting plant (Solanum) of Solanaceae with organic solvent such as ethanol.
A process for preparing a micro-amino acid compound fertilizer comprises the following steps:
s1 preparation of raw materials
Stirring 150 parts of plant straws by a crushing roller of a crusher at 300r/min, screening the crushed straw scraps, removing soil and impurities in the straw scraps, then putting the straw scraps into a fermentation kettle, adding 40 parts of water, heating the fermentation kettle to 300 ℃, continuously steaming at 300 ℃ for 50min, and evaporating the water to dryness to obtain the straw scraps with the water content of 80%.
S2 preparation of fermentation
Putting straw scraps with the water content of 80% into a fermentation kettle, setting the temperature in the fermentation kettle to 35 ℃, pouring 50 parts of amino acid solution into the fermentation kettle, continuously fermenting at the temperature of 30 ℃ for 20 hours, raising the temperature of the fermentation kettle to 120 ℃ after fermentation is completed, evaporating for 40min to evaporate water in the fermentation kettle, and evaporating the water content of a fermented product to 60% to obtain the rough micro amino acid compound fertilizer.
S3 disease-resistant treatment
And putting the obtained crude micro-amino acid compound fertilizer into a drying furnace, sequentially putting 30 parts of pinene, 10 parts of matrine and 5 parts of nicotine into the drying furnace, stirring the stirring shaft for 60min at 1000r/min to achieve the purpose of fully reducing half, finally heating the dryer to 200 ℃, stirring and drying for 50min to obtain the micro-amino acid compound fertilizer.
In summary, the micro-amino acid compound fertilizer and the preparation process thereof have the advantages that the pinene, the matrine and the nicotine are matched to ensure that crops using the micro-amino acid compound fertilizer have good antiviral property, the crops can be stimulated and adjusted to grow rapidly, the crops are promoted to grow strongly, the absorption of nutrient substances is promoted, meanwhile, the crops are prevented from being forced to be damaged by viruses, and the planting yield of the crops is effectively improved.
Pinene, matrine and nicotine extracted through botanicals can be well degraded, the problem that pesticide residues are eaten by a human body to cause discomfort is avoided, and simultaneously, the amino acid solution is added to further facilitate the absorption of crops to the micro-amino acid compound fertilizer, so that the aims of stimulating and adjusting the rapid growth of the crops, promoting the growth and the robustness of the crops and promoting the absorption of nutrient substances are better achieved.
The method has the advantages that the micro-amino acid compound fertilizer is obtained through the raw material straws, the cost of the micro-amino acid compound fertilizer can be effectively saved, the problem that the traditional straw burning pollutes the atmospheric environment can be effectively solved, the purpose of energy conservation is achieved to a certain extent, and the method has the characteristic of convenience in raw material selection.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (8)
1. The micro-amino acid compound fertilizer is characterized by comprising the following raw materials in parts by weight: 100-150 parts of plant straw, 20-50 parts of amino acid solution, 5-10 parts of zymocyte, 20-40 parts of water, 10-30 parts of pinene, 5-10 parts of matrine and 3-5 parts of nicotine.
2. The micro-amino acid compound fertilizer as claimed in claim 1, wherein the plant straw is one or more of soybean, corn, peanut, tomato, etc.
3. A micro-amino acid compound fertilizer as claimed in claim 1, wherein the amino acid solution is composed of 2-3 parts of indoleacetic acid solution, 1-3 parts of indolepropionic acid solution, 5-7 parts of naphthylacetic acid solution, 6-9 parts of methyl naphthylacetate and 4-8 parts of gibberellin solution, and the amino acid solution is obtained by mixing 2-3 parts of indoleacetic acid solution, 1-3 parts of indolepropionic acid solution, 5-7 parts of naphthylacetic acid solution, 6-9 parts of methyl naphthylacetate and 4-8 parts of gibberellin solution in a mixing device at 60-70 ℃ for 10-20 min, and finally standing for 5-10 min.
4. A micro-amino acid compound fertilizer as claimed in claim 1, wherein the fermentation tubes are composed of 5-10 parts of bacillus subtilis, 1-3 parts of cellulase, 2-4 parts of potassium perphosphate and 10-20 parts of distilled water, and the 5-10 parts of bacillus subtilis, 1-3 parts of cellulase, 2-4 parts of potassium perphosphate and 10-20 parts of distilled water are sequentially put into a fermentation kettle and fermented for 3-5 hours at a temperature of 30-35 ℃.
5. The micro-amino acid compound fertilizer as claimed in claim 1, wherein the pinene is obtained by fractionating a raw material selected from turpentine or white camphor oil.
6. The micro-amino acid compound fertilizer as claimed in claim 1, wherein the matrine is prepared by extracting dried roots, plants and fruits of Sophora flavescens ait of Leguminosae with organic solvent such as ethanol.
7. The micro amino acid compound fertilizer as claimed in claim 1, wherein the nicotine is extracted from a plant of Solanaceae (Solanum) with an organic solvent such as ethanol.
8. A process for preparing a micro-amino acid compound fertilizer is characterized by comprising the following steps:
s1 preparation of raw materials
Stirring 100-150 parts of plant straws by a crushing roller of a crusher at a speed of 200-300 r/min, screening crushed straw scraps, removing mud and impurities in the straw scraps, then putting the straw scraps into a fermentation kettle, adding 20-40 parts of water, heating the fermentation kettle to 200-300 ℃, continuously steaming at a high temperature of 200-300 ℃ for 30-50 min, and evaporating the water to obtain the straw scraps with a water content of 60-80%;
s2 preparation of fermentation
Putting straw scraps with the water content of 60-80% into a fermentation kettle, setting the temperature in the fermentation kettle to be 30-35 ℃, pouring 20-50 parts of amino acid solution into the fermentation kettle, continuously fermenting at the temperature of 25-30 ℃ for 10-20 hours, completing fermentation, raising the temperature of the fermentation kettle to 90-120 ℃, evaporating water in the fermentation kettle for 30-40 min, and evaporating the water content of a product obtained by fermentation to 40-60% to obtain a rough micro-amino acid compound fertilizer;
s3 disease-resistant treatment
Putting the obtained rough micro-amino acid compound fertilizer into a drying furnace, sequentially putting 10-30 parts of pinene, 5-10 parts of matrine and 3-5 parts of nicotine into the drying furnace, stirring the stirring shaft at 500-1000 r/min for 30-60 min to achieve the purpose of fully halving, finally heating the drying device to 100-200 ℃, stirring and drying for 40-50 min to obtain the micro-amino acid compound fertilizer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010250051.5A CN111269062A (en) | 2020-04-01 | 2020-04-01 | Micro-amino acid compound fertilizer and preparation process thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010250051.5A CN111269062A (en) | 2020-04-01 | 2020-04-01 | Micro-amino acid compound fertilizer and preparation process thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111269062A true CN111269062A (en) | 2020-06-12 |
Family
ID=70996188
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010250051.5A Pending CN111269062A (en) | 2020-04-01 | 2020-04-01 | Micro-amino acid compound fertilizer and preparation process thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111269062A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101116476A (en) * | 2007-08-23 | 2008-02-06 | 孟宪尧 | Poultry feedstuff for improving the alimentation of eggs |
| CN103274836A (en) * | 2013-06-09 | 2013-09-04 | 苏州仁成生物科技有限公司 | Special polyelement microorganism fertilizer for preventing yam anthracnose and preparation method of special polyelement microorganism fertilizer |
| CN105110894A (en) * | 2015-08-03 | 2015-12-02 | 陈宝娟 | Multi-functional biological organic bacterial fertilizer and production method therefor |
| CN105110996A (en) * | 2015-09-29 | 2015-12-02 | 黄尤 | Fertilizer special for navel orange and preparation method thereof |
-
2020
- 2020-04-01 CN CN202010250051.5A patent/CN111269062A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101116476A (en) * | 2007-08-23 | 2008-02-06 | 孟宪尧 | Poultry feedstuff for improving the alimentation of eggs |
| CN103274836A (en) * | 2013-06-09 | 2013-09-04 | 苏州仁成生物科技有限公司 | Special polyelement microorganism fertilizer for preventing yam anthracnose and preparation method of special polyelement microorganism fertilizer |
| CN105110894A (en) * | 2015-08-03 | 2015-12-02 | 陈宝娟 | Multi-functional biological organic bacterial fertilizer and production method therefor |
| CN105110996A (en) * | 2015-09-29 | 2015-12-02 | 黄尤 | Fertilizer special for navel orange and preparation method thereof |
Non-Patent Citations (2)
| Title |
|---|
| 何元胜等: "微生物肥料的作用机理及其应用前景", 《湖南农业科学》 * |
| 胡一鸿等: "《农业生物技术教程》", 31 August 2015, 西南交通大学出版社 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1872814A (en) | Method for preparing insect repelling organic fertilizer | |
| CN1054363C (en) | High nutrient composite fertilizer and production method | |
| CN108651160A (en) | A kind of method that waste mushroom leftover recycles culturing edible fungus | |
| CN101696127A (en) | Production process for manufacturing liquid fertilizer by using fish waste | |
| CN104072220B (en) | A kind of sweet wormwood biological organic fertilizer and preparation method thereof | |
| CN107409987A (en) | A kind of nutrient matrix and preparation method for dendrobium candidum soilless culture | |
| CN107827499A (en) | A kind of organic fertilizer for cane planting and preparation method thereof | |
| CN105060952A (en) | Amino acid microbial organic fertilizer | |
| CN110937942A (en) | Environment-friendly fertilizer and preparation method thereof | |
| CN104744160A (en) | Biocompound fertilizer for preventing and controlling sclerotinia and application method thereof | |
| CN105724055A (en) | Method for utilizing needle mushroom dregs to improve agaricus bisporus yield | |
| CN105474930A (en) | Organic green Chinese onion cultivation method | |
| CN109937975B (en) | Standardized earthworm breeding method | |
| CN110577449A (en) | Straw decomposed fertilizer and preparation method thereof | |
| CN112703850B (en) | Method for improving continuous cropping soil of hot peppers | |
| CN111269062A (en) | Micro-amino acid compound fertilizer and preparation process thereof | |
| CN102391032A (en) | Organic wheat medical fertilizer and preparation method thereof | |
| CN109369240A (en) | A kind of organic foliar fertilizer and preparation method thereof promoting photosynthesis of plant | |
| CN102391033B (en) | Organic corn medicinal fertilizer and preparation method thereof | |
| CN109206268A (en) | A kind of agrochemical and preparation method thereof | |
| CN115386498A (en) | Microbial compound microbial inoculant and method for producing organic fertilizer by utilizing mulberry silkworm breeding waste | |
| CN106946600A (en) | A kind of green planting method of tomato | |
| CN112919983A (en) | Root rot preventing liquid biological organic fertilizer and preparation method and application thereof | |
| CN108264425A (en) | A kind of organic medical fertilizer for preventing rice insect pest and preparation method thereof | |
| CN111233559A (en) | Production method and application of disease-resistant, insect-killing and yield-increasing organic fertilizer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200612 |