CN212315975U - Full-automatic inner loop amino acid liquid fertilizer apparatus for producing - Google Patents
Full-automatic inner loop amino acid liquid fertilizer apparatus for producing Download PDFInfo
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- CN212315975U CN212315975U CN202021164853.6U CN202021164853U CN212315975U CN 212315975 U CN212315975 U CN 212315975U CN 202021164853 U CN202021164853 U CN 202021164853U CN 212315975 U CN212315975 U CN 212315975U
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Abstract
The utility model discloses a full-automatic inner loop amino acid liquid fertilizer apparatus for producing, include along stoste storage tank, circulation that the material flow direction communicates in proper order dissolve feeding tank, chelate jar and produce the finished product storage tank, the top that the feeding tank was dissolved in the circulation is provided with the solid raw materials dog-house, and the discharge gate and the circulation of chelate jar dissolve feeding tank and still feed through circulation feed back pipeline. The utility model discloses circulation is thrown material dissolving tank and is thrown into amino acid hydrolysis stoste in a large number when throwing into compound such as microelement so as to restrain the sharp rising of temperature, and the internal circulation also can make compound such as microelement be unlikely to make chelation exothermic reaction too violent when gradually reaching saturation; the internal circulation can also accelerate chelation, and the chelation time is shortened by 1-2 hours under the same reaction condition.
Description
Technical Field
The utility model relates to an amino acid chelate fertilizer technical field, concretely relates to full-automatic inner loop amino acid liquid fertilizer apparatus for producing.
Background
The application of fertilizers in agricultural production to promote plant growth, increase yield and improve plant quality has become one of important measures, chemical fertilizers are widely applied by farmers at present, the chemical fertilizers have single components, high active ingredient content and good dispersibility, are easy to be absorbed and utilized by plants and are also called as 'quick-acting fertilizers', however, with the long-time and unreasonable application of the chemical fertilizers, the carbon-nitrogen ratio of soil is seriously disordered, the soil is hardened, the farming performance is poor, and some farmlands are even not suitable for secondary farming.
The amino acid fertilizer as a novel fertilizer can improve soil, solves the problem that the negative effects brought by chemical fertilizers are more and more widely accepted by people, particularly, the amino acid fertilizer prepared by hydrolyzing animal protein of dead livestock and poultry and slaughter wastes with diseases or unknown reasons has quick-acting function as well as chemical fertilizers, the implementation of the technical process can effectively consume the waste livestock and poultry and slaughter leftovers and produce high-quality amino acid organic fertilizer, the healthy development of upstream breeding industry can be effectively guaranteed, the production cost of the amino acid fertilizer and the bio-organic fertilizer can be greatly reduced, the development of downstream organic (class) fertilizer industry is promoted, and the sustainable cyclic utilization of resources is realized.
The chelation process of amino acid stock solution and compounds such as trace elements is accompanied with a certain amount of exothermic phenomenon, especially the exothermic reaction is violent in the feeding process, so that the temperature in the chelation tank is increased sharply. The temperature is one of the very important external conditions in the process of chelating trace elements by using the animal protein hydrolysis stock solution, and when the temperature exceeds a certain limit value, the quality of a chelated product is reduced and even the chelated product is scrapped. In addition, in the prior art, the animal proteolysis stock solution chelated trace element liquid fertilizer is generally fed by a conveying device or a high platform, namely, the material is conveyed to a chelating tank operation platform by the conveying device or a lifting device, 4-5 inorganic compounds are sequentially fed in a manual or mechanical mode according to the required amount, then a stirrer in the chelating tank is started to heat and stir, and the chelation is slowly carried out, wherein the chelation time is generally 4-6 hours. Because inorganic element has the hydroscopicity, lead to conveying equipment and high platform bonding material and be difficult for wasing and shovel off, cause the huge waste of manpower and financial resources, on the other hand is unfavorable for going on of extensive and automated production.
SUMMERY OF THE UTILITY MODEL
One of the purposes of the present invention is to overcome the defects existing in the prior art, and to provide a full-automatic internal circulation amino acid liquid fertilizer production device, which can make the compounds such as trace elements in the mixed raw materials gradually reach saturation and simultaneously not cause the exothermic reaction to be too violent.
In order to realize the technical effect, the utility model discloses a technical scheme does: the utility model provides a full-automatic inner loop amino acid liquid fertilizer apparatus for producing, includes along stoste storage tank, circulation that the material flow direction communicates in proper order dissolves feeding tank, chelate jar and produces the finished product storage tank, the top that the feeding tank was dissolved in the circulation is provided with the solid raw materials dog-house, the discharge gate of chelate jar with the feeding tank is dissolved in the circulation still through circulation feed back pipeline intercommunication. The pipeline which needs to overcome the gravity to lift the materials is connected with a lift pump.
The preferable technical scheme is that a cooling and stirring mechanism is arranged in the stock solution storage tank and/or the finished product storage tank. When the temperature in the tank is higher than a fixed value or the suspension degree of the materials is not enough, the cooling and stirring mechanism is started to fully stir the materials, so that the heat dissipation of the materials in the tank is accelerated correspondingly or the suspension degree of the materials is improved. As an equivalent alternative, it is also possible to provide stirring elements in the stock solution tank and/or the finished product tank and cooling units in the respective tank or on the pipe wall.
The cooling and stirring mechanism comprises a ventilation pipe, the ventilation pipe is communicated with an air outlet of the air blower through an air inlet pipe, and tangential ventilation holes are formed in the ventilation pipe. The wind hole of ventilation pipe is located under the liquid level, and the air current that the wind hole produced drives the liquid around the ventilation pipe and rotates around it, has the effect of accelerating heat dissipation and mixing material concurrently.
The preferable technical scheme is that a feed pipeline of the stock solution storage tank and a communicating pipeline between the chelating tank and the finished product storage tank are provided with filter components. Specifically, a coarse filter is arranged on a feed pipeline of the stock solution storage tank, and a fine filter is arranged on a communicating pipeline between the chelating tank and the finished product storage tank. The coarse filter and the fine filter are both filter devices for solid-liquid separation. Furthermore, in order to prevent the filter device from being blocked, a backflushing pipeline is further communicated with the filter assembly and comprises a single-backflushing liquid inlet pipe and a backflushing liquid outlet pipe, and backflushing fluid in the filter assembly is opposite to the flow direction of normal filtered fluid.
The preferable technical scheme is that a heating unit is arranged in the chelating tank or on the wall of the chelating tank. The heating unit can promote the material temperature in the chelate jar, promotes going on of compound and amino acid stoste chelation reaction such as microelement. The heating unit is a known component, and the selection range includes but is not limited to a steam pipe, an electric heating unit, a heat conduction oil pipe and a heating jacket.
The preferable technical scheme is that the heating unit comprises a jacket arranged on the wall of the chelating tank, an upper opening and a lower opening are arranged on the jacket, the upper opening is connected with a heating medium feeding pipe and a cooling medium returning pipe, and the lower opening is connected with the cooling medium feeding pipe and the heating medium returning pipe; the top of pressing from both sides the cover still is provided with the overflow pipe, be provided with the overflow valve on the overflow pipe. The jacket is used for heating and cooling, and the flow directions of the heating medium and the cooling medium in the jacket are opposite. When the cooling state of the chelating tank is switched to the heating state, the heating medium with higher temperature rises to the top of the jacket, and the cooling medium is driven to be discharged through the lower opening; when chelate jar heating state switches to cooling state, because the requirement for chelate reaction ambient temperature is high, consequently cold and hot medium switching time need tend to shorten the control, and coolant is detained at the clamp cover top by the feeding of clamp cover bottom, and part heating medium is detained in the actual production, derives this part heating medium through the overflow pipe, can reach rapid cooling's effect.
The compounds such as trace elements are generally inorganic fertilizers, are usually easy to dissolve in water, are easy to absorb moisture in the air to damp and agglomerate, and are blocked by using conveying equipment and lifting equipment, particularly in rainy days, and the damp performance of materials causes the belt or the spiral wall to be more viscous and thicker, so that equipment fails. The preferable technical scheme is that the circulating dissolving feeding tank is arranged in a pit, a solid raw material feeding mechanism is arranged on the ground, and the solid raw material feeding mechanism is connected with a solid raw material feeding port. The distance between the feed inlet and the solid raw material feeding mechanism can be shortened by the structure. Furthermore, the solid raw material feeding mechanism is an electronic metering conveying device suitable for solid materials, such as a spiral electronic scale, and a discharge port is in full-sealed flexible connection with a feed port of the circulating dissolving and feeding tank. Furthermore, the chelating tanks are added in parallel in a limited amount of modularization, and 6-20 chelating tanks can be circulated by one circulating dissolving feeding tank and the solid raw material feeding mechanism, so that large-scale automatic production is facilitated, feeding points of inorganic elements and exposure points in air can be reduced as far as possible, the feeding flow is shortened, the labor input and bonding waste are reduced, and the feeding mechanism is more convenient to clean and maintain.
The preferable technical scheme is that the periphery of a discharge pipeline and a circulating feed back pipeline between the circulating dissolving feeding tank and the chelating tank are respectively provided with a heat insulation layer.
The preferable technical proposal is that a one-way breather valve which is communicated from the outside of the tank to the inside of the tank is arranged on the circulating dissolving feeding tank and/or the chelating tank; and the stock solution storage tank, the finished product storage tank, the circulating dissolving feeding tank and the chelating tank are communicated with the deodorization system. The pressure of the air in the raw liquid storage tank and the finished product storage tank in the feeding process is larger than the pressure outside the tank, the pressure of the air in the tank in the discharging process is smaller than the pressure outside the tank, and the two-way breather valve can adjust the pressure inside and outside the tank in time. The stock solution storage tank, the circulating dissolving feeding tank, the chelating tank and the finished product storage tank are communicated with the deodorization system, and gas in the tanks is introduced into the deodorization system for treatment, so that the cleanness of the production environment is ensured. An exhaust pump can be arranged on an exhaust pipeline communicated with the deodorization system, so that the aim of active exhaust is fulfilled.
The production method of the full-automatic internal circulation amino acid liquid fertilizer is based on the full-automatic internal circulation amino acid liquid fertilizer production device, and comprises the following steps: introducing the solid raw materials and the amino acid stock solution in the stock solution storage tank into a circulating dissolving and feeding tank, discharging the mixed feed solution into a chelating tank, and carrying out internal circulating chelation on the chelating tank and the feed solution in the circulating dissolving and feeding tank; the solid feedstock comprises a compound of a trace element. Further, the solid raw material also comprises a pH value regulator.
The utility model has the advantages and the beneficial effects that:
the utility model discloses a full-automatic inner loop amino acid liquid fertilizer apparatus for producing the middle loop dissolves throws material jar and chelate jar seals inner loop structure, and the material is dissolved and the chelation process is all along with exothermic phenomenon, especially throws material process exothermic reaction and makes chelate material temperature sharply rise, the utility model discloses circulation is thrown material dissolving jar and can be dropped into amino acid hydrolysis stoste in a large number when dropping into compounds such as microelement so as to restrain exothermic temperature's sharp rise, and the inner loop also can make compounds such as microelement unlikely to make exothermic reaction too violent when progressively reaching the saturation;
the internal circulation can accelerate chelation, and the chelation time is shortened by 1-2 hours under the same reaction condition; the compounds which are not completely dissolved in the chelating tank can be returned to the circulating feeding dissolving tank through internal circulation, and the feeding amount of the amino acid stock solution can be adjusted to promote the amino acid stock solution to be fully dissolved, so that the content of the compounds which are not completely dissolved in the liquid fertilizer is reduced.
Drawings
FIG. 1 is a schematic view showing the construction of a full-automatic internal circulation amino acid liquid fertilizer production apparatus according to example 1;
FIG. 2 is a schematic view of the construction of the vent;
FIG. 3 is a cross-sectional view taken along A-A in FIG. 2;
FIG. 4 is a sectional view taken along line B-B in FIG. 2;
FIG. 5 is a schematic structural view of a full-automatic internal circulation amino acid liquid fertilizer production apparatus according to example 2;
FIG. 6 is a schematic view showing the construction of a circulating dissolving tank and an electronic metering device in example 3;
FIG. 7 is a schematic configuration diagram of a full-automatic internal circulation amino acid liquid fertilizer production apparatus according to example 4;
in the figure: 1. a stock solution storage tank; 2. a circulating dissolving feeding tank; 3. a chelating tank; 4. a finished product storage tank is produced; 5. a coarse filter; 6. a fine filter; 7. a spiral electronic scale; 8. an overflow pipe; 9. a vent pipe; 10. a blower.
Detailed Description
The following description will further describe embodiments of the present invention with reference to the accompanying drawings and examples. The following examples are only for illustrating the technical solutions of the present invention more clearly, and the protection scope of the present invention is not limited thereby.
Example 1
As shown in fig. 1 to 4, the full-automatic internal circulation amino acid liquid fertilizer production apparatus of embodiment 1 includes a stock solution storage tank 1, a circulation dissolution feeding tank 2, a chelating tank 3, and a finished product storage tank 4, which are sequentially communicated along a material flow direction, wherein a solid material feeding port 21 is provided at a top end of the circulation dissolution feeding tank 2, and a discharge port of the chelating tank 3 is communicated with the circulation dissolution feeding tank 2 through a circulation return pipeline.
A ventilation pipe 9 is arranged in the stock solution storage tank 1, the ventilation pipe 9 is communicated with an air outlet of an air blower 10 through an air inlet pipe, tangential air holes are formed in the pipe wall of the ventilation pipe 9, a bidirectional breather valve is arranged at the top of the stock solution storage tank 1, and the stock solution storage tank 1 is also communicated with a deodorization system; a discharge port on the side wall of the stock solution storage tank 1 is connected with a stock solution discharge pipe, and the stock solution discharge pipe is connected with a circulating dissolving feeding tank;
the top of the circulating dissolving and feeding tank 2 is provided with a one-way breather valve, a feed inlet for feeding compounds such as trace elements and the like and an exhaust port communicated with a deodorization system, and the one-way breather valve is communicated with the outside of the circulating dissolving and feeding tank 2 to the inside of the tank; a mechanical stirring piece is arranged in the circulating dissolving and feeding tank 2 to accelerate the dispersion and dissolution of compounds such as trace elements; the discharge port at the bottom of the circulating dissolving feeding tank 2 is communicated with the chelating tank 3 through a pipeline (connected with a discharge pump);
the wall of the chelating tank 3 is provided with a jacket, and the top of the chelating tank is also provided with a one-way breather valve communicated from the outside of the tank to the inside of the tank and an exhaust port communicated with the deodorization system; an upper opening of a jacket of the chelating tank 3 is connected with a heating medium feeding pipe and a cooling medium returning pipe, a lower opening of the jacket is connected with the cooling medium feeding pipe and the heating medium returning pipe, an overflow pipe 8 is further arranged at the top of the jacket, and an overflow valve is arranged on the overflow pipe 8; a discharge pipe communicated with a finished product storage tank 4 is arranged at the bottom of the chelating tank 3, a branch (a circulating feed back pipeline) of the discharge pipe is connected with a feed pipe of the circulating dissolving and feeding tank 2, and a mechanical stirring piece is arranged in the chelating tank to accelerate the dispersion and dissolution of compounds such as trace elements;
the top of the finished product storage tank 4 is provided with a bidirectional breather valve which is the same as the stock solution storage tank 1, the finished product storage tank 4 is communicated with a deodorization system, a ventilation pipe 9 is arranged in the tank body, and the ventilation pipe 9 is also communicated with an air outlet of an air blower 10 through an air inlet pipe.
In embodiment 1, the jacket is a heating and cooling common jacket, the heating medium introduced into the jacket is heating oil or steam, the cooling medium introduced into the jacket is cooled heat transfer oil or water, a heat exchange pipe is arranged in the cooling water tank, groundwater or water is injected into the cooling water tank, and the cooling medium feed pipe and the cooling medium return pipe are both connected with the heat exchange pipe. The amount of water in the cooling water tank must be sufficient to absorb the heat carried over by the cooling medium.
The compound feed of trace elements and the like in example 1 is a high-level feed using a screw electronic metering feed device, and the circulating dissolution feed tank 2 is located on the ground.
And heat insulation layers are arranged outside the discharge pipe from the circulating dissolving feeding tank 2 to the chelating tank 3 and the circulating return pipeline from the chelating tank 3 to the circulating dissolving feeding tank 2.
Example 2
As shown in fig. 5, embodiment 2 is based on embodiment 1, and is different in that a feed pipe of a stock solution storage tank 1 is communicated with a coarse filter 5, a discharge pipe between a chelating tank 3 and a finished product storage tank 4 is connected with a fine filter 6, and both the coarse filter 5 and the fine filter 6 are back-flushing filters, so that blockage faults can be timely treated. Through rough filtration and fine filtration, the solid content in the finished product of the amino acid chelated liquid fertilizer is reduced, and the liquid fertilizer is convenient for mechanized application and spraying of agricultural fertilization.
As known technique, a pump body is provided in the lifting line that needs to overcome the gravity of the material to ensure the normal supply of the material.
Example 3
As shown in FIG. 6, example 3 is based on example 1 except that in example 3, a circulating dissolution feeding tank 2 is provided in a pit, and a feed port for feeding a compound such as a trace element is directly connected to a screw electronic balance 7. Compared with the embodiment 1, the material conveying path in the embodiment 3 is short, the amount of moisture absorbed in the air is small, and the probability of equipment failure caused by the fact that the material is wetted and adhered to the wall is low.
Example 4
As shown in fig. 7, example 4 is based on example 3, except that the production apparatus of example 4 comprises a plurality of chelate tanks 3 (three in fig. 7), the chelate tanks 3 each forming an internal circulation with a circulating dissolving feed tank 2, and a plurality of product storage tanks 4 (two in fig. 7) communicating with the chelate tanks 3.
The production process of the amino acid liquid fertilizer comprises the following steps: the amino acid stock solution led out from the previous procedure enters a stock solution storage tank 1, and the liquid level height of the stock solution storage tank 1 is controlled; when the temperature of the material in the stock solution storage tank 1 is too high, the air blower 10 blows air into the stock solution storage tank 1 through the air inlet pipe and the ventilation pipe 9, the airflow of the ventilation pipe 9 is ejected along the tangential direction of the wall of the ventilation pipe to drive the material to rotate, and the accelerated motion of the material is beneficial to the acceleration of heat dissipation; air is blown in to cause the gas pressure in the stock solution storage tank 1 to increase, and the gas (containing amino acid peculiar smell generated by materials) in the stock solution storage tank 1 is discharged into a deodorization system through a deodorization pipeline; when the pressure in the stock solution storage tank 1 is increased due to the activity of microorganisms, the bidirectional breather valve exhausts outwards; when the gas pressure in the stock solution storage tank 1 is smaller than the pressure outside the tank, the two-way breather valve supplies air into the tank to enable the pressure inside and outside the tank to tend to be balanced;
adding amino acid stock solution (discharged from a stock solution storage tank 1) and solid trace element compounds (fed at a certain feeding speed by a spiral electronic scale 7) into the circulating dissolving and feeding tank 2 in proportion, starting a mechanical stirrer in the circulating dissolving and feeding tank 2, dissolving and mixing the amino acid stock solution and the trace element compounds in the tank, and discharging the mixture into a chelating tank 3; the unidirectional breather valve replenishes air outside the tank into the tank, and when the pressure in the tank is higher than the pressure outside the tank, gas is continuously discharged through a pressure reducing valve on the top of the tank, and the circulating dissolving feeding tank 2 is communicated with the deodorization pipeline;
the liquid fertilizer which is completely reacted in the chelating tank 3 is discharged into a finished product storage tank, the liquid fertilizer is the same as the raw liquid storage tank 1, the temperature of materials in the finished product storage tank 4 is adjusted through a vent pipe 9, the air pressure is adjusted through a bidirectional breather valve, and a deodorization system processes air discharged from the finished product storage tank 4.
The production method of example 2 is based on example 1, with the difference that the amino acid stock solution entering the stock solution storage tank is first subjected to rough filtration; the liquid fertilizer discharged from the bottom of the chelating tank 3 is subjected to fine filtration. When the coarse filtering equipment and the fine filtering equipment are blocked, the filtered materials are led out for backflushing.
The production method of example 3 is the same as example 1.
Example 4 during operation, the discharge of circulation dissolving feeding tank 2 is led into a plurality of chelating tanks 3, and a plurality of chelating tanks 3 and circulation dissolving feeding tank 2 respectively form an internal circulation. Example 4 meets the requirements of large-scale production based on the same capacity of the chelation tank 3 and the recycle dissolution feed tank 2.
The amino acid liquid fertilizer introduced into the product tank 4 in examples 1 to 4 was further introduced into a packaging line.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of improvements and decorations can be made without departing from the technical principle of the present invention, and these improvements and decorations should also be regarded as the protection scope of the present invention.
Claims (9)
1. The utility model provides a full-automatic inner loop amino acid liquid fertilizer apparatus for producing, includes along the stoste storage tank, circulation that the material flow direction communicates in proper order dissolves feeding tank, chelate jar and produces the finished product storage tank, the top that the feeding tank was dissolved in the circulation is provided with solid raw materials dog-house, its characterized in that, the discharge gate of chelate jar with the feeding tank is dissolved in the circulation still feeds through circulation feed back pipeline.
2. The full-automatic internal circulation amino acid liquid fertilizer production device of claim 1, wherein a cooling and stirring mechanism is arranged in the stock solution storage tank and/or the finished product storage tank.
3. The full-automatic internal circulation amino acid liquid fertilizer production device according to claim 2, wherein the cooling and stirring mechanism comprises a ventilation pipe, the ventilation pipe is communicated with an air outlet of an air blower through an air inlet pipe, and tangential ventilation holes are formed in the ventilation pipe.
4. The apparatus for producing amino acid liquid fertilizer with full-automatic internal circulation according to claim 1, wherein a feed pipeline of the stock solution storage tank and a communication pipeline between the chelate tank and the product storage tank are provided with a filter assembly.
5. The full-automatic internal circulation amino acid liquid fertilizer production device according to claim 1, wherein the inside of the chelate tank or the wall of the chelate tank is provided with a heating unit.
6. The full-automatic internal circulation amino acid liquid fertilizer production device according to claim 5, wherein the heating unit comprises a jacket arranged on the wall of the chelating tank, the jacket is provided with an upper opening and a lower opening, the upper opening is connected with the heating medium feeding pipe and the cooling medium returning pipe, and the lower opening is connected with the cooling medium feeding pipe and the heating medium returning pipe; the top of pressing from both sides the cover still is provided with the overflow pipe, be provided with the overflow valve on the overflow pipe.
7. The full-automatic internal circulation amino acid liquid fertilizer production device according to claim 1, wherein the circulation dissolving feeding tank is arranged in a pit, and a solid raw material feeding mechanism is arranged on the ground and connected with the solid raw material feeding port.
8. The full-automatic production device of amino acid liquid fertilizer with internal circulation as claimed in claim 1, wherein the discharge pipeline and the circulation return pipeline between the circulation dissolving feeding tank and the chelating tank are provided with heat insulation layers on the periphery.
9. The full-automatic production device of amino acid liquid fertilizer with internal circulation as claimed in claim 1, wherein the circulating dissolving and feeding tank and/or the chelating tank is provided with a one-way breather valve for communicating the outside of the tank to the inside of the tank; and the stock solution storage tank and/or the finished product storage tank are/is provided with a two-way breather valve, and the stock solution storage tank, the finished product storage tank, the circulating dissolving feeding tank and the chelating tank are communicated with a deodorization system.
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| CN202021164853.6U CN212315975U (en) | 2020-06-22 | 2020-06-22 | Full-automatic inner loop amino acid liquid fertilizer apparatus for producing |
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| CN202021164853.6U CN212315975U (en) | 2020-06-22 | 2020-06-22 | Full-automatic inner loop amino acid liquid fertilizer apparatus for producing |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| 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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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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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