CN112430149A - Production method of amino enzyme immune disease-resistant fertilizer - Google Patents
Production method of amino enzyme immune disease-resistant fertilizer Download PDFInfo
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- CN112430149A CN112430149A CN202011331785.2A CN202011331785A CN112430149A CN 112430149 A CN112430149 A CN 112430149A CN 202011331785 A CN202011331785 A CN 202011331785A CN 112430149 A CN112430149 A CN 112430149A
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- waste liquid
- immune disease
- liquid
- resistant fertilizer
- amino
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C3/00—Fertilisers containing other salts of ammonia or ammonia itself, e.g. gas liquor
-
- 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
-
- 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
- C05G5/00—Fertilisers characterised by their form
- C05G5/10—Solid or semi-solid fertilisers, e.g. powders
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Pest Control & Pesticides (AREA)
- Fertilizers (AREA)
Abstract
A production method of an amino enzyme immune disease-resistant fertilizer belongs to the field of microbial metabolite treatment. The invention aims to solve the problem of environmental protection of waste treatment which is difficult to solve by liquid waste of a microorganism production plant, and the method comprises the following steps: uniformly mixing 25-30% of yeast waste liquid, 25-30% of lactobacillus waste liquid, 20-25% of photosynthetic bacteria waste liquid and 20-25% of bacillus subtilis waste liquid according to the mass percent, then adding ammonium sulfate accounting for 15-20% of the total mass of the waste liquid, and fully chelating at 25-30 ℃ to form reaction liquid; spraying the chelating reaction solution to a cylindrical hot air dryer at the temperature of 800-1000 ℃ for drying. The invention uniformly recovers and mixes the waste liquid which is difficult to be treated by the factory for producing the saccharomycetes, the lactic acid bacteria, the photosynthetic bacteria and the bacillus subtilis, carries out amino chelation reaction, and further processes the waste liquid into the macro-element immune disease-resistant fertilizer, thereby not only solving the problem of waste liquid treatment of the microbial fermentation factory, but also providing the high-quality macro-element immune disease-resistant fertilizer for agricultural production.
Description
Technical Field
The invention belongs to the field of microbial metabolite treatment, and particularly relates to a production method of an amino enzyme immune disease-resistant fertilizer.
Background
The method for producing the bacterial powder by using the microbial liquid for fermentation and then adopting the methods of filtering, centrifuging, decompressing and low-temperature drying is widely applied to daily life, medicine and agricultural production of people. Generally, 3 tons of waste liquid can be generated when 1 ton of bacteria powder is produced in the production of the bacteria powder, a large amount of liquid waste can be discharged after a production enterprise invests a large amount of capital to carry out environment-friendly treatment, and a large amount of investment and waste of manpower and material resources of the bacteria powder production enterprise are caused. Because most of the wastes are acidic, production enterprises generally adopt the mode of temporarily storing the wastes in a large cement pool, directly discharging the wastes after simple sedimentation and neutralization reaction, and some enterprises even directly discharge the wastes without treatment, thereby causing serious pollution to the environment. However, the liquid waste contains a large amount of beneficial components, including organic matters, amino acids, polysaccharides, humic acids and the like, which are all useful substances for crops in agricultural production and have an important effect on improving the disease resistance of the crops.
Disclosure of Invention
The invention aims to solve the problem of environmental protection in waste treatment which is difficult to solve by liquid waste in a microorganism production plant, and provides a method for producing an amino enzyme immune disease-resistant fertilizer.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a production method of an amino ferment immune disease-resistant fertilizer comprises the following steps:
the method comprises the following steps: uniformly mixing 25-30% of yeast waste liquid, 25-30% of lactobacillus waste liquid, 20-25% of photosynthetic bacteria waste liquid and 20-25% of bacillus subtilis waste liquid according to the mass percent, then adding ammonium sulfate accounting for 15-20% of the total mass of the waste liquid, and fully chelating at 25-30 ℃ to form reaction liquid;
step two: spraying the chelating reaction solution to a cylindrical hot air dryer at the temperature of 800-1000 ℃ for drying.
Compared with the prior art, the invention has the beneficial effects that: the invention solves the problem of environmental protection treatment of waste liquid which is difficult to treat in yeast, lactic acid bacteria, photosynthetic bacteria and bacillus subtilis plants, the waste liquid after extraction of yeast, lactic acid bacteria, photosynthetic bacteria and bacillus subtilis powder is mixed and then undergoes amino chelation reaction, a spray instantaneous drying method is utilized to evaporate water, and a large amount of amino lactic acid, amino polysaccharide and amino humic acid powder mixture is separated out to become amino ferment, thereby providing a high-quality macroelement immune disease-resistant water-soluble fertilizer for agricultural production.
Detailed Description
The technical solutions of the present invention are further described below, but not limited thereto, and modifications or equivalent substitutions may be made to the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention.
The first embodiment is as follows: the embodiment records a production method of an amino enzyme immune disease-resistant fertilizer, which comprises the following steps:
the method comprises the following steps: recovering waste liquid which is difficult to treat in a yeast, lactic acid bacteria, photosynthetic bacteria and bacillus subtilis factory, uniformly mixing 25-30% of yeast waste liquid, 25-30% of lactic acid bacteria waste liquid, 20-25% of photosynthetic bacteria waste liquid and 20-25% of bacillus subtilis waste liquid according to mass percent, adding ammonium sulfate accounting for 15-20% of the total mass of the waste liquid, and fully chelating at 25-30 ℃ to form reaction liquid;
step two: the chelating reaction solution is sprayed to a cylindrical hot air dryer at the temperature of 800-1000 ℃ for drying, water is evaporated instantly, a large amount of amino lactic acid, amino polysaccharide and amino humic acid powder are separated out from the chelating reaction solution to form amino enzyme, the amino enzyme has an immune effect on the disease resistance of crops, and the high N, P, K content can be prepared into a macroelement immune disease-resistant water-soluble fertilizer.
The method comprises the steps of recovering waste liquid which is difficult to treat in a yeast, lactic acid bacteria, photosynthetic bacteria and bacillus subtilis factory, wherein the content of lactic acid, amino acid and humic acid in the yeast waste liquid and the lactic acid bacteria waste liquid is high, and the polysaccharide in the photosynthetic bacteria waste liquid and the bacillus subtilis waste liquid is high, so that more reaction products are formed, generally, 25-30% of the yeast waste liquid, 25-30% of the lactic acid bacteria waste liquid, 20-25% of the photosynthetic bacteria waste liquid and 20-25% of the bacillus subtilis waste liquid are uniformly mixed, ammonium sulfate which accounts for 15-20% of the total mass of the waste liquid is added, the mixture can be heated to 25-30 ℃ under normal pressure and fully chelated to form reaction liquid, on one hand, the chelation reaction can be smoothly completed under the temperature condition, and on the; cellulase, ligninase, and the like. The chelating reaction liquid is sprayed to a 800-.
The second embodiment is as follows: in the first step, 25% of yeast waste liquid, 25% of lactic acid bacteria waste liquid, 25% of photosynthetic bacteria waste liquid and 25% of bacillus subtilis waste liquid are uniformly mixed according to the mass percentage, then ammonium sulfate accounting for 20% of the total mass of the waste liquid is added, and the mixture is fully chelated at 30 ℃ to form the reaction liquid.
The third concrete implementation mode: in the first step, 30% of yeast waste liquid, 30% of lactic acid bacteria waste liquid, 20% of photosynthetic bacteria waste liquid and 20% of bacillus subtilis waste liquid are uniformly mixed according to the mass percentage, then ammonium sulfate accounting for 15% of the total mass of the waste liquid is added, and the mixture is fully chelated at 28 ℃ to form the reaction liquid.
The fourth concrete implementation mode: in the second step, the chelation reaction solution is sprayed to a 1000 ℃ cylindrical hot air dryer for drying.
The fifth concrete implementation mode: in the second step, the chelation reaction solution is sprayed to a 800 ℃ cylindrical hot air dryer for drying.
Claims (5)
1. The production method of the amino enzyme immune disease-resistant fertilizer is characterized by comprising the following steps: the method comprises the following steps:
the method comprises the following steps: uniformly mixing 25-30% of yeast waste liquid, 25-30% of lactobacillus waste liquid, 20-25% of photosynthetic bacteria waste liquid and 20-25% of bacillus subtilis waste liquid according to the mass percent, then adding ammonium sulfate accounting for 15-20% of the total mass of the waste liquid, and fully chelating at 25-30 ℃ to form reaction liquid;
step two: spraying the chelating reaction solution to a cylindrical hot air dryer at the temperature of 800-1000 ℃ for drying.
2. The method for producing the amino enzyme immune disease-resistant fertilizer according to claim 1, wherein the amino enzyme immune disease-resistant fertilizer comprises the following steps: in the first step, 25% of yeast waste liquid, 25% of lactic acid bacteria waste liquid, 25% of photosynthetic bacteria waste liquid and 25% of bacillus subtilis waste liquid are uniformly mixed according to the mass percentage, then ammonium sulfate accounting for 20% of the total mass of the waste liquid is added, and the mixture is fully chelated at 30 ℃ to form reaction liquid.
3. The method for producing the amino enzyme immune disease-resistant fertilizer according to claim 1, wherein the amino enzyme immune disease-resistant fertilizer comprises the following steps: in the first step, 30% of yeast waste liquid, 30% of lactic acid bacteria waste liquid, 20% of photosynthetic bacteria waste liquid and 20% of bacillus subtilis waste liquid are uniformly mixed according to the mass percentage, then ammonium sulfate accounting for 15% of the total mass of the waste liquid is added, and the mixture is fully chelated at 28 ℃ to form reaction liquid.
4. The method for producing the amino enzyme immune disease-resistant fertilizer according to claim 1, wherein the amino enzyme immune disease-resistant fertilizer comprises the following steps: and in the second step, spraying the chelation reaction liquid to a cylindrical hot air dryer at 1000 ℃ for drying.
5. The method for producing the amino enzyme immune disease-resistant fertilizer according to claim 1, wherein the amino enzyme immune disease-resistant fertilizer comprises the following steps: and in the second step, spraying the chelation reaction liquid to a cylindrical hot air dryer at 800 ℃ for drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011331785.2A CN112430149A (en) | 2020-11-24 | 2020-11-24 | Production method of amino enzyme immune disease-resistant fertilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011331785.2A CN112430149A (en) | 2020-11-24 | 2020-11-24 | Production method of amino enzyme immune disease-resistant fertilizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112430149A true CN112430149A (en) | 2021-03-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011331785.2A Pending CN112430149A (en) | 2020-11-24 | 2020-11-24 | Production method of amino enzyme immune disease-resistant fertilizer |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3725029A (en) * | 1971-09-27 | 1973-04-03 | Ga Pacific Corp | Preparation of ammonium sulfate fertilizer constituent |
| CN105294183A (en) * | 2014-06-16 | 2016-02-03 | 上海绿乐生物科技有限公司 | Multifunctional liquid biological fertilizer and production method therefor |
-
2020
- 2020-11-24 CN CN202011331785.2A patent/CN112430149A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3725029A (en) * | 1971-09-27 | 1973-04-03 | Ga Pacific Corp | Preparation of ammonium sulfate fertilizer constituent |
| CN105294183A (en) * | 2014-06-16 | 2016-02-03 | 上海绿乐生物科技有限公司 | Multifunctional liquid biological fertilizer and production method therefor |
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Application publication date: 20210302 |
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