CN203360311U - Novel device for producing high-potassium water flush fertilizer containing amino acid chelated secondary and micro elements - Google Patents
Novel device for producing high-potassium water flush fertilizer containing amino acid chelated secondary and micro elements Download PDFInfo
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- CN203360311U CN203360311U CN 201320455123 CN201320455123U CN203360311U CN 203360311 U CN203360311 U CN 203360311U CN 201320455123 CN201320455123 CN 201320455123 CN 201320455123 U CN201320455123 U CN 201320455123U CN 203360311 U CN203360311 U CN 203360311U
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Abstract
The utility model discloses a novel device for producing a high-potassium water flush fertilizer containing amino acid chelated secondary and micro elements, and belongs to the field of compound fertilizers. The device comprises a concentration tank, a filtering machine, a pulverizer, a chemical reaction kettle, an atomizer, a dryer and a mixing machine, wherein an amino acid mother solution inlet is formed in the concentration tank; a first slurry pump and a pipeline I are arranged between the concentration tank and the filtering machine, and an impurity outlet is formed in the filtering machine; a second slurry pump and a pipeline II are arranged between the filtering machine and the chemical reaction kettle, and a sodium hydroxide aqueous solution inlet and a lignin inlet are formed in the chemical reaction kettle; calcium, magnesium, copper, iron, manganese, zinc, boron and molybdenum inlets and potassium sulphate and potassium nitrate inlets are formed in the pulverizer; a first conveyor is arranged between the pulverizer and the chemical reaction kettle; a third slurry pump and a pipeline III are arranged between the chemical reaction kettle and the atomizer which is directly connected with the dryer; a second conveyor is arranged between the dryer and the mixing machine; and a third conveyor is arranged between the pulverizer and the mixing machine, and a finished product outlet is formed in the mixing machine.
Description
Technical field
The utility model belongs to the production of compound fertilizer field, relates in particular to a kind of novel containing micro-high potassium punching fertilising production equipment in chelating amino acids.
Background technology
Liquid fertilizer is again in the punching fertilising, it is soluble in water the readily avaiable fertilizer of solid and is applied fertilizer in the mode of water band fertilizer, the characteristics of punching fertilising be a kind of can be fully water-soluble, and promptly be dissolved in the water, very easily by farm crop, absorbed, and its absorption rate is relatively high, more crucial is it can be applied to spray, drip, the agricultural facility such as filling, realize water-fertilizer integral, reach water-saving, economize usefulness fertile, the saving of labor.The main component of punching fertilising is nitrogenous fertilizer and potash fertilizer, and nitrogenous fertilizer and potash fertilizer water-soluble strong by the rich water combination, allows the nitrogen potassium nutrition of solubility infiltrate in soil, then be the crop root absorption.Along with the refinement to the research of farm crop nutrient uptake feature, all kinds of fertilizer of producing in recent years all will add trace element, especially chelated microelements, generally speaking, the punching fertilising can contain the needed whole nutritive elements of crop growth and trace element, so, people can carry out component design according to the Different Crop needed nutritional needs characteristics of growing fully, and can according to the different growing ways of crop, to fertilizer formula, make adjustment at any time.The utility model is exactly the mechanism that a kind of production contains the high potassium punching of aminoacid chelating microelement fertilising, and this installs with concentration tank, filter, pulverizer, chemical reaction kettle, spraying gun, drying machine, the blending machine is equipment, take that to produce amino acid whose byproduct span amino acid mother liquor be carrier, first and quantitative moderate-element calcium, magnesium and trace copper, iron, manganese, zinc, boron, molybdenum, through chelatropic reaction, makes middle trace element be converted into solubleness good, and easily trace element in chelating amino acids state absorbed by crops, then pass through atomization, be dried to powder, then with the monoammonium phosphate of formula ratio, vitriolate of tartar, the high potassium powdery punching fertilising that the raw materials such as saltpetre are made through the post-treatment that is mixed, products characteristics is 100% entirely water-soluble, be particularly suitable for the cash crop such as gourd, fruit and vegetable, can meet the crops such as gourd, fruit and vegetable in the phase of bearing fruit the demand to potassium and other nutrient, there is the raising utilization rate of fertilizer, obvious effect of increasing production, the advantage such as application process is easy, it can be along with irrigation water with sprinkling irrigation, drip irrigation, when the modes such as pouring are irrigated, fertilising, both saved water, saved again fertilizer, but also saved a large amount of labor forces, and because the application process of water soluble fertilizer is application with irrigation water, institute is so that fertilising is very even.
Summary of the invention
Being to provide that the utility model mainly solves is a kind of novel containing micro-high potassium punching fertilising production equipment in chelating amino acids, this device is with concentration tank, filter, pulverizer, chemical reaction kettle, spraying gun, drying machine, the blending machine is equipment, with span amino acid mother liquor, calcium, magnesium, copper, iron, manganese, zinc, boron, molybdenum, xylogen, monoammonium phosphate, vitriolate of tartar, saltpetre is raw material, obtain trace element in the chelating amino acids state after the chelatropic reaction of span amino acid mother liquor and middle trace element, then pass through atomization, be dried to powder, again and monoammonium phosphate, vitriolate of tartar, after being mixed, the raw materials such as saltpetre make finished product.
The technical solution adopted in the utility model is:
A kind of novel containing micro-high potassium punching fertilising production equipment in chelating amino acids, comprising: concentration tank 1, filter 2, pulverizer 3, chemical reaction kettle 4, spraying gun 5, drying machine 6, blending machine 7, it is characterized in that: concentration tank 1 is provided with span amino acid mother liquor import 8, 2, concentration tank 1 and filter are provided with the first shurry pump and pipeline 9, filter 2 is provided with impurity outlet 10, 4 of filter 2 and chemical reaction kettles are provided with the second shurry pump and pipeline 11, chemical reaction kettle 4 is provided with aqueous sodium hydroxide solution import 12, xylogen import 13, pulverizer 3 is provided with calcium, magnesium, copper, iron, manganese, zinc, boron, molybdenum import 14, monoammonium phosphate, vitriolate of tartar, saltpetre import 15, 4 of pulverizer 3 and chemical reaction kettles are provided with the first transfer roller 16, 5, chemical reaction kettle 4 and spraying gun are provided with the 3rd shurry pump and pipeline 17, spraying gun 5 directly is connected with drying machine 6, 7, drying machine 6 and blending machine are provided with second conveyor 18, 7, pulverizer 3 and blending machine are provided with the 3rd transfer roller 19, blending machine 7 is provided with product outlet 20.
Further technical scheme of the present utility model is:
Described whole shurry pump is that stainless steel shurry pump, pipeline are polyethylene pipe.
Described whole transfer roller is scraper conveyor.
The beneficial effects of the utility model are: provide a kind of novel containing micro-high potassium punching fertilising production equipment in chelating amino acids, this apparatus structure is reasonable, production technique is simple, pollution-free waste discharge, in the product chelating amino acids, micro-high potassium punching fertilising has 100% entirely water-soluble, be particularly suitable for the cash crop such as gourd, fruit and vegetable in the phase of bearing fruit the demand to potassium and other nutrient, there is the raising utilization rate of fertilizer, obvious effect of increasing production, the advantage such as application process is easy.
The accompanying drawing explanation:
As Fig. 1 is structure iron of the present utility model.
Embodiment
Embodiment:
Further illustrate and use the particular content of this new device production containing micro-high potassium punching fertilising most preferred embodiment in chelating amino acids below in conjunction with accompanying drawing:
1. the span amino acid mother liquor of formula ratio is sent in concentration tank 1 by the span amino acid mother liquor import 8 be arranged on concentration tank 1, adjust the temperature in concentration tank 1 to be concentrated between 90 ℃-95 ℃, concentration time is 6-8 hour, while being concentrated into 23-25 ° of B é, stop concentrating, send into filter 2 filtrations by the first shurry pump and the pipeline 9 that are arranged at 2, concentration tank 1 and filter immediately, the purpose of filtering is removal of impurities, the impurity of removing is discharged by the impurity outlet 10 be arranged on filter 2, then the span amino acid mother liquor after filtering is sent into to chemical reaction kettle 4 by the second shurry pump and the pipeline 11 that are arranged at 4 of filter 2 and chemical reaction kettles.
2. the middle trace elements calcium of formula ratio, magnesium, copper, iron, manganese, zinc, boron, molybdenum are sent into to pulverizer 3 to carry out after the solid phase pulverization process obtaining the middle trace element pulverized stand-by by being arranged at calcium, magnesium, copper, iron, manganese, zinc, boron, molybdenum import 14 on pulverizer 3.
3. by microwave heating method, the temperature of chemical reaction kettle 4 interior span amino acid mother liquors is brought up to 75-85 ℃, start agitator, by the first transfer roller 16 that is arranged at 4 of pulverizer 3 and chemical reaction kettles, the middle trace element after pulverizing is sent into to chemical reaction kettle 4, chelatropic reaction starts, now to constantly monitor the pH value, the pH value that adds aqueous sodium hydroxide solution to control chemical reaction kettle 4 interior reaction solutions by the aqueous sodium hydroxide solution import 12 be arranged on chemical reaction kettle 4 remains between 5-7, after 6-7 hour chelatropic reaction time, chelatropic reaction finishes, now by being arranged at the stablizer xylogen of the import 13 interpolation formula ratios on chemical reaction kettle 4, stirring reaction stops after 0.2 hour stirring, obtain trace element in liquid chelating amino acids.
4. trace element in liquid chelating amino acids is sent into to spraying gun 5 atomizations by the 3rd shurry pump and the pipeline 17 that are arranged at 5, chemical reaction kettle 4 and spraying gun, directly send into drying machine 6 dryings after atomization, drying temperature is 45-55 ℃, be 1.2-1.5 hour time of drying, obtain trace element in Powdered chelating amino acids after drying, send into blending machine 7 by the second conveyor 18 that is arranged at 7, drying machine 6 and blending machine immediately.
5. the monoammonium phosphate of formula ratio, vitriolate of tartar, saltpetre are sent into to pulverizer 3 pulverizing by the monoammonium phosphate, vitriolate of tartar, the saltpetre import 15 that are arranged on pulverizer 3, after pulverizing and powder send into blending machine 7 by the 3rd transfer roller 19 that is arranged at 7, pulverizer 3 and blending machine, all material even blend in blending machine 7 are got product, get final product by product outlet 20 dischargings that are arranged on blending machine 7.
Claims (3)
- One kind novel containing micro-high potassium punching fertilising production equipment in chelating amino acids, comprising: concentration tank (1), filter (2), pulverizer (3), chemical reaction kettle (4), spraying gun (5), drying machine (6), blending machine (7), it is characterized in that: concentration tank (1) is provided with span amino acid mother liquor import (8), be provided with the first shurry pump and pipeline (9) between concentration tank (1) and filter (2), filter (2) is provided with impurity outlet (10), be provided with the second shurry pump and pipeline (11) between filter (2) and chemical reaction kettle (4), chemical reaction kettle (4) is provided with aqueous sodium hydroxide solution import (12), xylogen import (13), pulverizer (3) is provided with calcium, magnesium, copper, iron, manganese, zinc, boron, molybdenum import (14), monoammonium phosphate, vitriolate of tartar, saltpetre import (15), be provided with the first transfer roller (16) between pulverizer (3) and chemical reaction kettle (4), be provided with the 3rd shurry pump and pipeline (17) between chemical reaction kettle (4) and spraying gun (5), spraying gun (5) directly is connected with drying machine (6), be provided with second conveyor (18) between drying machine (6) and blending machine (7), be provided with the 3rd transfer roller (19) between pulverizer (3) and blending machine (7), blending machine (7) is provided with product outlet (20).
- 2. according to claim 1 a kind of novel containing micro-high potassium punching fertilising production equipment in chelating amino acids, it is characterized in that: described whole shurry pumps are that stainless steel shurry pump, pipeline are polyethylene pipe.
- 3. according to claim 1 a kind of novel containing micro-high potassium punching fertilising production equipment in chelating amino acids, it is characterized in that: described whole transfer rollers are scraper conveyor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320455123 CN203360311U (en) | 2013-07-29 | 2013-07-29 | Novel device for producing high-potassium water flush fertilizer containing amino acid chelated secondary and micro elements |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320455123 CN203360311U (en) | 2013-07-29 | 2013-07-29 | Novel device for producing high-potassium water flush fertilizer containing amino acid chelated secondary and micro elements |
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| Publication Number | Publication Date |
|---|---|
| CN203360311U true CN203360311U (en) | 2013-12-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320455123 Expired - Fee Related CN203360311U (en) | 2013-07-29 | 2013-07-29 | Novel device for producing high-potassium water flush fertilizer containing amino acid chelated secondary and micro elements |
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| Country | Link |
|---|---|
| CN (1) | CN203360311U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105315061A (en) * | 2014-07-31 | 2016-02-10 | 沣田宝农业科技有限公司 | Integrated equipment for chelating secondary and trace nutrient elements |
| CN111592430A (en) * | 2020-06-22 | 2020-08-28 | 江阴市鹏鹞联业生物科技有限公司 | Full-automatic internal circulation amino acid liquid fertilizer production device and production method |
-
2013
- 2013-07-29 CN CN 201320455123 patent/CN203360311U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105315061A (en) * | 2014-07-31 | 2016-02-10 | 沣田宝农业科技有限公司 | Integrated equipment for chelating secondary and trace nutrient elements |
| CN111592430A (en) * | 2020-06-22 | 2020-08-28 | 江阴市鹏鹞联业生物科技有限公司 | Full-automatic internal circulation amino acid liquid fertilizer production device and production method |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131225 Termination date: 20140729 |
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| EXPY | Termination of patent right or utility model |