CN217068888U - Production equipment for polyglutamic acid chelated calcium - Google Patents
Production equipment for polyglutamic acid chelated calcium Download PDFInfo
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- CN217068888U CN217068888U CN202221001921.6U CN202221001921U CN217068888U CN 217068888 U CN217068888 U CN 217068888U CN 202221001921 U CN202221001921 U CN 202221001921U CN 217068888 U CN217068888 U CN 217068888U
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- calcium
- reaction tank
- polyglutamic acid
- retort
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Abstract
The utility model is suitable for a preparation field that biological chelate was fertile provides a production facility for polyglutamic acid chelate calcium, smash mixing arrangement including retort and calcium source, still include: the stirring assembly comprises a motor and a stirring shaft arranged in the reaction tank, and one end of the stirring shaft, which is far away from the reaction tank, is connected with the output end of the motor; the feeding part comprises a first feeding port and a second feeding port which are arranged at the top of the reaction tank; and discharge material portion, discharge material portion sets up in the one end that the feed portion was kept away from to the retort, discharge material portion includes the bin outlet of being connected with the retort, be provided with control flap on the bin outlet, the utility model discloses in, the device is through the abundant chelation reaction with polyglutamic acid and calcium for carboxyl, amino etc. in calcium ion and the polyglutamic acid molecule combine, what polyglutamic acid chelate calcium can be better is absorbed by the plant and is utilized, thereby promotes the plant to the absorption of calcium.
Description
Technical Field
The utility model belongs to the preparation field of biological chelate fertilizer, especially, relate to a production facility for polyglutamic acid chelated calcium.
Background
Calcium is an indispensable element for crop growth, and due to the development of agriculture and the change of farmer concept, calcium fertilizer is more and more commonly used and the usage amount is more and more increased. Firstly, calcium is an important component element of crop cell walls, can promote division of epidermal cells and improve toughness and thickness of fruit epidermis, thereby accelerating growth of fruit epidermis and avoiding fruit cracking caused by the fact that the growth speed of fruit peels cannot keep pace with the growth speed of fruit pulp. And secondly, the calcium element can regulate the permeability of plant cell membranes and reduce the synthesis of ethylene in crops, thereby delaying the weakening speed of the crops and improving the fruiting period of the crops. In addition, calcium is alkaline as a metal ion, can effectively relieve soil acidification, eliminate organic acid secreted by a root system, and stabilize the surrounding environment of the root system of crops, thereby inhibiting the impregnation of various harmful germs on the root system and reducing the occurrence of diseases.
However, the traditional calcium fertilizers on the market such as quicklime, calcium superphosphate, calcium magnesium phosphate, calcium nitrate and the like are easily fixed by soil after being applied to the soil, and cannot play an effective role; later-appearing EDTA calcium is not easy to decompose, has large environmental pollution, strong toxicity, relatively large molecular weight and low absorptivity; the sugar alcohol calcium can be transported in the xylem phloem of the crops doubly, so that the absorption rate is improved, but the sugar alcohols are various and have different effects. Most of them have not solved the problem that they are easily fixed by soil and easily react with phosphorus-containing fertilizers.
The poly calcium glutamate is a novel chelated calcium fertilizer, can overcome the defects of the products, is not easy to be fixed by soil, can be well separated after being absorbed by plants, and can effectively improve the utilization rate of calcium. However, many of the currently commercially available calcium polyglutamates are not stable enough, have low calcium content, and have the problem of reaction with sulfate and phosphate. Therefore, how to improve the stability of the production process, improve the calcium content and produce stable polyglutamic acid calcium chelate is a key problem to be solved.
SUMMERY OF THE UTILITY MODEL
An object of the embodiment of the utility model is to provide a production facility for polyglutamic acid chelated calcium aims at solving the polyglutamic acid calcium product of production on the market at present, and is a lot of stable inadequately, and calcium content is low to can appear the problem with sulfate radical and phosphate radical reaction.
The embodiment of the utility model provides a realize like this, a production facility for polyglutamic acid chelated calcium, smash mixing arrangement including retort and calcium source, still include:
the stirring assembly comprises a motor and a stirring shaft arranged in the reaction tank, a plurality of stirring claws are arranged on the stirring shaft, and one end of the stirring shaft, which is far away from the reaction tank, is connected with the output end of the motor;
the feeding part comprises a first feeding port and a second feeding port which are arranged at the top of the reaction tank; and
the discharge portion, the discharge portion sets up in the one end that the feed portion was kept away from to the retort, the discharge portion includes the bin outlet of being connected with the retort, be provided with control valve on the bin outlet.
According to the further technical scheme, the calcium source smashing and mixing device is connected with the reaction tank through a material conveying belt, and one end, far away from the material conveying belt, of the material conveying belt is located right above the first feeding port.
According to a further technical scheme, the side wall of the reaction tank is further provided with a temperature control assembly, the temperature control assembly comprises a jacket, and a water filling port and a steam inlet hole are formed in the jacket.
According to a further technical scheme, a thermometer used for monitoring the temperature inside the reaction tank is further arranged on the side wall of the reaction tank.
The embodiment of the utility model provides a pair of production facility for polyglutamic acid chelated calcium, in will adding the retort through the second charge door polyglutamic acid liquid earlier during the use, then with the starter motor, it is rotatory to drive the (mixing) shaft through the motor, and the (mixing) shaft drives the stirring claw and mixes the stirring to the inside liquid of retort, then lets in high temperature steam and heats the retort in the cover toward pressing from both sides through the steam inlet. And then conveying the crushed and uniformly mixed calcium source in the calcium source crushing and mixing device to a first feeding port through a material conveying belt, slowly adding the calcium source into the reaction tank, and controlling the steam amount to maintain the temperature in the chelation reaction tank between 60 and 65 ℃ because the reaction is endothermic. And after the calcium source is added, continuously stirring and reacting for 4-8 hours to fully perform the chelation reaction, then introducing cold water from a water filling port to cool, and discharging the polyglutamic acid chelated calcium through a discharge port after cooling. The device is through the abundant chelation reaction with polyglutamic acid and calcium for the carboxyl in calcium ion and the polyglutamic acid molecule, amino etc. group combines, and the two chelate together, can prevent that calcium ion from being fixed by phosphate radical and sulfate radical etc. in the soil, reduce the calcium and run off, what polyglutamic acid chelate calcium can be better is absorbed by the plant and is utilized, thereby promotes the absorption of plant to calcium.
Drawings
Fig. 1 is a schematic structural diagram of a production apparatus for calcium polyglutamate chelate according to an embodiment of the present invention.
In the drawings: a reaction tank 1; a stirring shaft 2; a motor 3; a first feed inlet 4; a second feed inlet 5; a thermometer 6; a jacket 7; a water filling port 8; a steam inlet 9; a discharge opening 10; a control valve 11; a calcium source pulverizing and mixing device 12; a material conveying belt 13; and a stirring claw 14.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
The following detailed description is provided for the specific embodiments of the present invention.
As shown in fig. 1, a production apparatus for chelated calcium polyglutamate provided by an embodiment of the present invention includes a reaction tank 1 and a calcium source crushing and mixing device 12, and further includes:
the stirring assembly comprises a motor 3 and a stirring shaft 2 arranged in the reaction tank 1, a plurality of stirring claws 14 are arranged on the stirring shaft 2, and one end of the stirring shaft 2 far away from the reaction tank 1 is connected with the output end of the motor 3;
the feeding part comprises a first feeding port 4 and a second feeding port 5 which are arranged at the top of the reaction tank 1; and
the discharge portion, the discharge portion sets up in retort 1 one end of keeping away from the feed portion, the discharge portion includes the bin outlet 10 of being connected with retort 1, be provided with control valve 11 on the bin outlet 10.
The embodiment of the utility model provides an in, earlier add polyglutamic acid liquid through second charge door 5 in retort 1 during the use, then with starter motor 3, it is rotatory to drive (mixing) shaft 2 through motor 3, and (mixing) shaft 2 drives stirring claw 14 and mixes the stirring to 1 inside liquid of retort, then heats retort 1. And then conveying the crushed and uniformly mixed calcium source in the calcium source crushing and mixing device 12 to the first feeding port 4, slowly adding the crushed and uniformly mixed calcium source into the reaction tank 1, and controlling the steam amount to maintain the temperature in the chelation reaction tank between 60 and 65 ℃ because the reaction is endothermic. And after the calcium source is added, continuously stirring and reacting for 4-8 hours to fully perform the chelation reaction, then cooling the reaction tank 1, and discharging the polyglutamic acid chelated calcium through a discharge outlet 10 after cooling.
As shown in fig. 1, as a preferred embodiment of the present invention, the calcium source pulverizing and mixing device 12 is connected to the reaction tank 1 through a material conveying belt 13, and one end of the material conveying belt 13, which is far away from the calcium source pulverizing and mixing device 12, is located right above the first feeding port 4.
The embodiment of the utility model provides an in, then carry the calcium source of the crushing mixing in the mixing arrangement 12 to first charge door 4 departments through material conveyer belt 13 with the calcium source, slowly add inside retort 1, can control the addition in calcium source through the speed of control material conveyer belt 13.
As shown in fig. 1, as a preferred embodiment of the present invention, the sidewall of the reaction tank 1 is further provided with a temperature control assembly, the temperature control assembly includes a jacket 7, and the jacket 7 is provided with a water filling opening 8 and a steam inlet 9.
The embodiment of the utility model provides an in, let in high temperature steam and heat retort 1 in pressing from both sides cover 7 through steam inlet 9, after the chelation reaction fully carried out, let in cold water from the filler 8 and cool down retort 1, the polyglutamic acid chelate calcium after the cooling alright emit through bin outlet 10.
As shown in fig. 1, as a preferred embodiment of the present invention, the sidewall of the reaction tank 1 is further provided with a thermometer 6 for monitoring the temperature inside the reaction tank 1, so that the temperature of the reaction tank 1 is adjusted by the temperature displayed by the thermometer 6.
During the use earlier add polyglutamic acid liquid through second charge door 5 in retort 1, then with starter motor 3, drive (mixing) shaft 2 rotation through motor 3, the (mixing) shaft 2 drives stirring claw 14 and mixes the stirring to the liquid of retort 1 inside, then lets in high temperature steam to heat retort 1 in pressing from both sides cover 7 through steam inlet 9. Then, the crushed and uniformly mixed calcium source in the calcium source crushing and mixing device 12 is conveyed to the first feeding port 4 through the material conveying belt 13 and is slowly added into the reaction tank 1, and the steam amount is controlled to maintain the temperature in the chelation reaction tank between 60 ℃ and 65 ℃ because the reaction is endothermic. And after the calcium source is added, continuously stirring and reacting for 4-8 hours to fully perform the chelation reaction, then introducing cold water from a water filling port 8 for cooling, and opening a control valve 11 after cooling to discharge the polyglutamic acid chelated calcium through a discharge port 10.
The above description is only exemplary of the present invention and should not be taken as limiting the scope of the present invention, as any modifications, equivalents, improvements and the like made within the spirit and principles of the present invention are intended to be included within the scope of the present invention.
Claims (5)
1. The utility model provides a production facility for polyglutamic acid chelated calcium, includes retort and the crushing mixing arrangement of calcium source, its characterized in that still includes:
the stirring assembly comprises a motor and a stirring shaft arranged in the reaction tank, and one end of the stirring shaft, which is far away from the reaction tank, is connected with the output end of the motor;
the feeding part comprises a first feeding port and a second feeding port which are arranged at the top of the reaction tank; and
the discharge portion, the discharge portion sets up in the one end that the feed portion was kept away from to the retort, the discharge portion includes the bin outlet of being connected with the retort, be provided with control valve on the bin outlet.
2. The production equipment for the polyglutamic acid chelated calcium as claimed in claim 1, wherein the calcium source crushing and mixing device is connected with the reaction tank through a material conveying belt, and one end of the material conveying belt, which is far away from the material conveying belt, is positioned right above the first feeding port.
3. The production equipment for the polyglutamic acid chelated calcium as claimed in claim 2, wherein a temperature control assembly is further arranged on the side wall of the reaction tank, the temperature control assembly comprises a jacket, and a water filling port and a steam inlet hole are arranged on the jacket.
4. The apparatus for producing poly (calcium glutamate) -chelate according to claim 2, wherein said side wall of said reaction tank is further provided with a thermometer for monitoring the temperature inside said reaction tank.
5. The production equipment for the polyglutamic acid chelated calcium as claimed in claim 2, wherein a plurality of stirring claws are arranged on the stirring shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221001921.6U CN217068888U (en) | 2022-04-27 | 2022-04-27 | Production equipment for polyglutamic acid chelated calcium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221001921.6U CN217068888U (en) | 2022-04-27 | 2022-04-27 | Production equipment for polyglutamic acid chelated calcium |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217068888U true CN217068888U (en) | 2022-07-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221001921.6U Active CN217068888U (en) | 2022-04-27 | 2022-04-27 | Production equipment for polyglutamic acid chelated calcium |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217068888U (en) |
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2022
- 2022-04-27 CN CN202221001921.6U patent/CN217068888U/en active Active
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