CN205313422U - Water -soluble fertile production system of macroelement - Google Patents
Water -soluble fertile production system of macroelement Download PDFInfo
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- CN205313422U CN205313422U CN201521116155.8U CN201521116155U CN205313422U CN 205313422 U CN205313422 U CN 205313422U CN 201521116155 U CN201521116155 U CN 201521116155U CN 205313422 U CN205313422 U CN 205313422U
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Abstract
The utility model relates to a water -soluble fertile production system of macroelement belongs to the water -soluble fertile technical field of manufacturing, including retort no. 1 and retort no. 2, the discharge gate of retort no. 1 and the feed inlet of retort no. 2 link to each other, a retort upper end is equipped with ammonia admission pipe and phosphoric acid by wet process inlet pipe, two upper ends of retort are equipped with the macroelement inlet pipe, be equipped with filter equipment on retort no. 1 and the retort connecting pipe between two, two lower extreme discharge gates of retort are connected with concentrated jar of heating, the lower extreme discharge gate that the heating is concentrated jar is connected with the cooling crystallizer, cooling crystallizer upper end is equipped with the microelement inlet pipe, the discharge gate of cooling crystallizer lower extreme is established ties and is had centrifuge and packagine machine. The utility model discloses simple structure, the cost is lower, can guarantee that water content not tolerant and impurity is controllable, the pH valve of control product that can be fine, the ammonia can cyclic utilization, heating efficiency is high, can the accurate control temperature, and the crystalline solid in the cooling crystallizer can conveniently be discharged.
Description
Technical field
This utility model belongs to Water soluble fertilizer manufacturing technology field, is specifically related to a kind of a great number of elements Water soluble fertilizer production system.
Background technology
A great number of elements water-soluble fertilizer is a kind of containing a great number of elements N P and K, it is possible to completely soluble water solublity Chemical Mixed Fertilizer. It is through water dissolution or dilution, can be used for fertigation (including the modes such as sprinkling irrigation, drip irrigation), the liquid or solid product of the purposes such as root is dipped in foliage dressing, soilless culture, seed soaking. Using the both using water wisely of a great number of elements water-soluble fertilizer, save again fertilising, and plant absorption is fast, absorption rate is high, comprehensive nutrition, instant effect.
The research of Water soluble fertilizer is started late by China, now it is in that in the production process of a great number of elements Water soluble fertilizer, the major part simple physical mixture that still application mountain vallage is workshop-based produces, such equipment contains more impurity, bad control acid-base value, being unfavorable for controlling temperature, the discharging of crystalline solid is not easily discharged; Mostly complex additionally for the external equipment introduced, cause relatively costly, be unfavorable for marketing.
Utility model content
The purpose of this utility model is to provide a kind of a great number of elements Water soluble fertilizer production system, solves the problems referred to above.
This utility model a great number of elements Water soluble fertilizer production system, including retort one and retort two, the discharging opening of retort one is connected with the charging aperture of retort two, it is provided with stirring vane in retort one and retort two, stirring vane connects stirring motor one by shaft, retort one upper end is provided with ammonia and enters pipe and phosphoric acid by wet process feed pipe, retort two upper end is provided with a great number of elements feed pipe, connecting tube between retort one and retort two is provided with defecator, retort two lower end discharging opening is connected to heating concentration tank, the lower end discharging opening of heating concentration tank is connected to crystallisation by cooling tank, heating concentration tank upper end is provided with Ammonia recovery mouth, Ammonia recovery mouth connects back to closed tube, recovery tube other end coupled reaction tank one, recovery tube is provided with filtration drying device, crystallisation by cooling tank upper end is provided with trace element feed pipe, it is provided with cooling coil inside crystallisation by cooling tank, square stirring vane it is provided with inside cooling coil, square stirring vane is fastened on the stirring motor two of crystallisation by cooling upper end, the discharging opening of crystallisation by cooling tank lower end is in series with centrifuge and packer.
The external rings of described heating concentration tank is wound with electromagnetic heating coil, and the efficiency of heating surface is high, it is possible to precise control of temperature, the outside of electromagnetic heating coil is coated with heat-insulation layer.
Described heating concentration tank side is respectively arranged with backflow feed tube and backflow drain pipe up and down, and backflow feed tube and backflow drain pipe junction are provided with reflux pump, are provided with agitating device inside heating concentration tank so that concentration speed is faster.
Connecting tube between described heating concentration tank and crystallisation by cooling tank is provided with the pump housing, accelerates material charging rate.
Compared with prior art, the utility model has the advantage of:
System structure is simple, less costly, it can be ensured that not tolerant and impurity the content of water is controlled, it is possible to well controlling the acid-base value of product, ammonia can recycle; Heating concentration tank uses Electromagnetic Heating, and the efficiency of heating surface is high, it is possible to precise control of temperature, the crystalline solid in crystallisation by cooling tank can conveniently be discharged.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure: 1, ammonia enters pipe, 2, phosphoric acid by wet process feed pipe, 3, retort one, 4, defecator, 5, a great number of elements feed pipe, 6, retort two, 7, filtration drying device, 8, recovery tube, 9, heating concentration tank, 10, electromagnetic heating coil, 11, backflow drain pipe, 12, heat-insulation layer, 13, reflux pump, 14, trace element feed pipe, 15, stirring motor two, 16, crystallisation by cooling tank, 17, cooling coil, 18, square stirring vane, 19, centrifuge, 20, packer, 21, backflow feed tube, 22, stirring motor one, 23, agitating device.
Detailed description of the invention
Below against accompanying drawing, detailed description of the invention of the present utility model is described in further detail.
A great number of elements Water soluble fertilizer production system as shown in Figure 1, including retort 1 and retort 26, the discharging opening of retort 1 is connected with the charging aperture of retort 26, it is provided with stirring vane in retort 1 and retort 26, stirring vane connects stirring motor 1 by shaft, retort 1 upper end is provided with ammonia and enters pipe 1 and phosphoric acid by wet process feed pipe 2, retort 26 upper end is provided with a great number of elements feed pipe 5, connecting tube between retort 1 and retort 26 is provided with defecator 4, retort 26 lower end discharging opening is connected to heating concentration tank 9, the lower end discharging opening of heating concentration tank 9 is connected to crystallisation by cooling tank 16, heating concentration tank 9 upper end is provided with Ammonia recovery mouth, Ammonia recovery mouth connects back to closed tube 8, recovery tube 8 other end coupled reaction tank 1, recovery tube 8 is provided with filtration drying device 7, crystallisation by cooling tank 16 upper end is provided with trace element feed pipe 14, crystallisation by cooling tank 16 is internal is provided with cooling coil 17, square stirring vane 18 it is provided with inside cooling coil 17, square stirring vane 18 is fastened on the stirring motor 2 15 on crystallisation by cooling tank 16 top, the discharging opening of crystallisation by cooling tank 16 lower end is in series with centrifuge 19 and packer 20.
The external rings of heating concentration tank 9 is wound with electromagnetic heating coil 10, and the efficiency of heating surface is high, it is possible to precise control of temperature, the outside of electromagnetic heating coil 10 is coated with heat-insulation layer 12.
Heating concentration tank 9 side is respectively arranged with backflow feed tube 21 and backflow drain pipe 11 up and down, and backflow feed tube 21 and backflow drain pipe 11 junction are provided with reflux pump 13, and heating concentration tank 9 is internal is provided with agitating device 23 so that concentration speed is faster.
Connecting tube between heating concentration tank 9 and crystallisation by cooling tank 16 is provided with the pump housing, accelerates material charging rate.
In sum, this utility model system structure is simple, less costly, it can be ensured that not tolerant and impurity the content of water is controlled, it is possible to well controlling the acid-base value of product, ammonia can recycle; Heating concentration tank uses Electromagnetic Heating, and the efficiency of heating surface is high, it is possible to precise control of temperature, the crystalline solid in crystallisation by cooling tank can conveniently be discharged.
Claims (4)
1. an a great number of elements Water soluble fertilizer production system, including retort one (3) and retort two (6), the discharging opening of retort one (3) is connected with the charging aperture of retort two (6), it is provided with stirring vane in retort one (3) and retort two (6), stirring vane connects stirring motor one (22) by shaft, it is characterized in that retort one (3) upper end is provided with ammonia and enters pipe (1) and phosphoric acid by wet process feed pipe (2), retort two (6) upper end is provided with a great number of elements feed pipe (5), connecting tube between retort one (3) and retort two (6) is provided with defecator (4), retort two (6) lower end discharging opening is connected to heating concentration tank (9), the lower end discharging opening of heating concentration tank (9) is connected to crystallisation by cooling tank (16), heating concentration tank (9) upper end is provided with Ammonia recovery mouth, Ammonia recovery mouth connects back to closed tube (8), recovery tube (8) other end coupled reaction tank one (3), recovery tube (8) is provided with filtration drying device (7), crystallisation by cooling tank (16) upper end is provided with trace element feed pipe (14), crystallisation by cooling tank (16) is internal is provided with cooling coil (17), cooling coil (17) inner side is provided with square stirring vane (18), square stirring vane (18) is fastened on the stirring motor two (15) on crystallisation by cooling tank (16) top, the discharging opening of crystallisation by cooling tank (16) lower end is in series with centrifuge (19) and packer (20).
2. a great number of elements Water soluble fertilizer production system according to claim 1, it is characterized in that the external rings of described heating concentration tank (9) is wound with electromagnetic heating coil (10), the outside of electromagnetic heating coil (10) is coated with heat-insulation layer (12).
3. a great number of elements Water soluble fertilizer production system according to claim 1 and 2, it is characterized in that described heating concentration tank (9) side is respectively arranged with backflow feed tube (21) and backflow drain pipe (11) up and down, backflow feed tube (21) and backflow drain pipe (11) junction are provided with reflux pump (13), and heating concentration tank (9) is internal is provided with agitating device (23).
4. a great number of elements Water soluble fertilizer production system according to claim 1, it is characterised in that the connecting tube between described heating concentration tank (9) and crystallisation by cooling tank (16) is provided with the pump housing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521116155.8U CN205313422U (en) | 2015-12-29 | 2015-12-29 | Water -soluble fertile production system of macroelement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521116155.8U CN205313422U (en) | 2015-12-29 | 2015-12-29 | Water -soluble fertile production system of macroelement |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205313422U true CN205313422U (en) | 2016-06-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521116155.8U Active CN205313422U (en) | 2015-12-29 | 2015-12-29 | Water -soluble fertile production system of macroelement |
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| Country | Link |
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| CN (1) | CN205313422U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109985595A (en) * | 2019-04-11 | 2019-07-09 | 嘉施利（新疆）水溶肥有限公司 | A kind of no outlet Water soluble fertilizer reaction system |
| CN112295525A (en) * | 2020-09-09 | 2021-02-02 | 湖北达亨农业科技发展有限公司 | Device and method for producing efficient instant water-soluble fertilizer by using byproduct nitric acid |
-
2015
- 2015-12-29 CN CN201521116155.8U patent/CN205313422U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109985595A (en) * | 2019-04-11 | 2019-07-09 | 嘉施利（新疆）水溶肥有限公司 | A kind of no outlet Water soluble fertilizer reaction system |
| CN109985595B (en) * | 2019-04-11 | 2021-06-01 | 嘉施利（新疆）水溶肥有限公司 | Water-soluble fertilizer reaction system without external drainage |
| CN112295525A (en) * | 2020-09-09 | 2021-02-02 | 湖北达亨农业科技发展有限公司 | Device and method for producing efficient instant water-soluble fertilizer by using byproduct nitric acid |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |