CN220327935U - Centrifugal drying device is used in glyphosate production - Google Patents
Centrifugal drying device is used in glyphosate production Download PDFInfo
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- CN220327935U CN220327935U CN202321857298.9U CN202321857298U CN220327935U CN 220327935 U CN220327935 U CN 220327935U CN 202321857298 U CN202321857298 U CN 202321857298U CN 220327935 U CN220327935 U CN 220327935U
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- drying
- centrifugal
- guide ring
- drying device
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- 238000001035 drying Methods 0.000 title claims abstract description 112
- 239000005562 Glyphosate Substances 0.000 title claims abstract description 43
- XDDAORKBJWWYJS-UHFFFAOYSA-N glyphosate Chemical compound OC(=O)CNCP(O)(O)=O XDDAORKBJWWYJS-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 229940097068 glyphosate Drugs 0.000 title claims abstract description 43
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- 239000007921 spray Substances 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims description 15
- 210000001503 joint Anatomy 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 22
- 238000010438 heat treatment Methods 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000003595 mist Substances 0.000 description 4
- 239000011344 liquid material Substances 0.000 description 3
- 238000000889 atomisation Methods 0.000 description 2
- 238000005485 electric heating Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000001694 spray drying Methods 0.000 description 2
- 101100298225 Caenorhabditis elegans pot-2 gene Proteins 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a centrifugal drying device for glyphosate production, which comprises a drying tank and a centrifugal atomizer, wherein the centrifugal atomizer is movably arranged at the upper end position inside the drying tank, a hot air blower is fixedly arranged at one side of the drying tank, the hot air blower and the drying tank are in through connection through a hot air pipe, a guide ring for auxiliary drying is arranged at the middle position inside the drying tank, a plurality of groups of exhaust spray heads are fixedly arranged inside the guide ring, the exhaust ends of the exhaust spray heads are obliquely arranged, and a conical top cover is arranged at the lower part inside the drying tank; by means of the arrangement of the guide ring and the annular air holes, a gas heating structure can be formed in the middle of the drying tank, and when the glyphosate material in solution passes through the middle of the drying tank, the glyphosate material in the un-dried solution can be heated for the second time, so that a granular structure is formed, the drying rate of the centrifugal drying device is improved, and the centrifugal drying device is provided with an auxiliary drying structure.
Description
Technical Field
The utility model belongs to the technical field of glyphosate processing, and particularly relates to a centrifugal drying device for glyphosate production.
Background
The centrifugal drying device is mainly applied to the drying and forming of liquid materials, is most suitable for generating powdery or granular solid products from emulsion, solution, suspension and pumpable pasty liquid raw materials, and mainly comprises a high-speed centrifugal atomizer and a hot air device.
Patent document CN103239878A discloses a centrifugal spray drying apparatus comprising: drying tower body, feed arrangement and cyclone, feed arrangement, drying tower body and cyclone are between communicate in proper order, feed arrangement includes feed inlet, filter and feeding nozzle, feed inlet, filter and feeding nozzle connect gradually, pass through the pipe connection between drying tower body and the cyclone, the pipeline inner wall is provided with dry adsorbed layer. Through the mode, the centrifugal spray drying device can improve drying efficiency, and is simple in structure, convenient to use and convenient to discharge.
The centrifugal drying device has certain defects when in use, has low drying rate and does not have a multiple drying structure, and when the liquid material is discharged in a centrifugal mode in a mist liquid state, part of the mist liquid is not heated sufficiently, so that the liquid is still discharged in a liquid state, and the use effect is poor; and when the centrifugal drying device runs, the atomized liquid is dried and heated through high-temperature air, and the heat is directly discharged to the outside, so that the centrifugal drying device has no thermal cycle structure, the self power consumption of the centrifugal drying device is increased, and the centrifugal drying device has single functionality.
Disclosure of Invention
The utility model solves the problems that:
1. the centrifugal drying device has low drying rate and no multiple drying structure, and when the liquid material is discharged in a centrifugal mode in a mist liquid state, part of the mist liquid is not heated sufficiently, so that the liquid is still discharged in a liquid state, and the use effect is poor;
2. and when the centrifugal drying device runs, the atomized liquid is dried and heated through high-temperature air, and the heat is directly discharged to the outside, so that the centrifugal drying device has no thermal cycle structure, the self power consumption of the centrifugal drying device is increased, and the centrifugal drying device has single functionality.
The aim of the utility model can be achieved by the following technical scheme:
the utility model provides a centrifugal drying device is used in glyphosate production, includes drying cylinder and centrifugal atomizer, centrifugal atomizer movable mounting is in the inside upper end position of drying cylinder, one side fixed mounting of drying cylinder has the air heater, link up through the hot-blast main between air heater and the drying cylinder, the inboard middle part position of drying cylinder is equipped with the water conservancy diversion ring that is used for carrying out auxiliary drying, the inboard fixed mounting of water conservancy diversion ring has a plurality of groups exhaust shower nozzle, the exhaust end of exhaust shower nozzle is the slope setting, the inboard lower part position of drying cylinder is provided with the toper top cap, the discharge end of toper top cap and drying cylinder is fixed through the discharging pipe butt joint, the side of toper top cap is provided with two sets of blast pipes.
As a further technical scheme of the utility model, two groups of exhaust pipes are arranged side by side, the conical top cover and the air inlet end of the air heater are fixedly connected through the exhaust pipes, and hot air exhausted from the drying tank can be recovered by utilizing the arrangement of the exhaust pipes, so that the power consumption of the air heater is reduced.
According to the technical scheme, annular air holes are formed in the guide ring, a plurality of groups of exhaust spray heads are arranged on the inner side of the guide ring in an annular array, the air heating structure can be formed in the middle of the drying tank by means of the arrangement of the guide ring and the cooperation of the annular air holes, and when the glyphosate material in solution state passes through the middle of the drying tank, the glyphosate material in un-dried solution state can be heated for the second time, so that a granular structure is formed.
According to the technical scheme, a connecting pipe is fixedly arranged on the outer surface of one end of the guide ring, the guide ring and the hot air pipe are fixedly connected through the connecting pipe in a butt joint mode, hot air exhausted by the hot air pipe is led into the guide ring through the arrangement of the connecting pipe, and is exhausted through an exhaust nozzle of the guide ring.
According to the technical scheme, a raw material barrel is arranged on one side of the drying tank, a feeding pipe is arranged at the upper end of the raw material barrel, a pump is arranged at the upper end of the drying tank, the feeding pipe is in butt joint with the feeding end of the pump, and glyphosate materials in solution in the raw material barrel can be pumped through the feeding pipe by the aid of the pump.
As a further technical scheme of the utility model, a feeding groove is arranged in the middle of the outer surface of the upper end of the drying tank, and a receiving bin is arranged at the bottom of the conical top cover.
The utility model has the beneficial effects that: according to the centrifugal drying device for the production of the glyphosate, when the centrifugal drying device is used, an auxiliary drying structure is formed in the middle of a drying tank, mist-like liquid is fully heated, the drying effect of the glyphosate is improved, during operation, a user starts a pump to enable the pump to pump a raw material barrel through a feeding pipe, so that the glyphosate material in solution in the raw material barrel is pumped out, the glyphosate material in solution is guided into the centrifugal atomizer, the centrifugal atomizer rotates at a high speed, the glyphosate material in solution is sprayed out in an atomization state, the user starts a hot air machine, the hot air machine is matched with a hot air pipe to introduce hot air into the drying tank in an electric heating mode, the glyphosate material in the atomization state is quickly coagulated into a powdery solid structure after being heated in the drying tank, a gas heating structure can be formed in the middle of the drying tank by matching with an annular air hole through the arrangement of the guide ring, and when the glyphosate material in solution passes through the middle of the drying tank, the glyphosate material in solution can be secondarily heated, so that a granular structure is formed, the glyphosate material in solution is promoted, and the drying device has the auxiliary drying structure;
through setting up the blast pipe, when this centrifugal drying device is used in glyphosate production, be linked together the intake pipe of blast pipe and air heater for the air heater has heat recovery structure, utilizes the setting of blast pipe, can retrieve the interior exhaust steam of drying pot, thereby reduces the consumption of air heater, makes the heat that retrieves reintroduce into the air heater, reduces this centrifugal drying device is used in glyphosate production's energy consumption, promotes its result of use.
Drawings
The present utility model is further described below with reference to the accompanying drawings for the convenience of understanding by those skilled in the art.
FIG. 1 is a schematic diagram of the structure of the present utility model;
FIG. 2 is a plan view of the deflector ring of the present utility model;
fig. 3 is an overall construction view of the conical top cover of the present utility model.
In the figure: 1. a raw material barrel; 2. a drying tank; 3. a guide ring; 4. a centrifugal atomizer; 5. a feed pipe; 6. a pump machine; 7. a feed chute; 8. a hot air pipe; 9. a discharge pipe; 10. an air heater; 11. an exhaust pipe; 12. a conical top cover; 13. a material receiving bin; 14. an exhaust nozzle; 15. a connecting pipe; 16. annular air holes.
Detailed Description
The technical solutions of the present utility model will be clearly and completely described in connection with the embodiments, and it is obvious that the described embodiments are only some embodiments of the present utility model, not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
As shown in figures 1-3, a centrifugal drying device for glyphosate production comprises a drying tank 2 and a centrifugal atomizer 4, wherein the centrifugal atomizer 4 is movably arranged at the upper end position inside the drying tank 2, one side of the drying tank 2 is fixedly provided with a hot air blower 10, the hot air blower 10 is in through connection with the drying tank 2 through a hot air pipe 8, the middle position inside the drying tank 2 is provided with a guide ring 3 for auxiliary drying, the inner side of the guide ring 3 is fixedly provided with a plurality of groups of exhaust spray heads 14, the exhaust ends of the exhaust spray heads 14 are obliquely arranged, the lower position inside the drying tank 2 is provided with a conical top cover 12, the conical top cover 12 and the discharge end of the drying tank 2 are fixedly connected through a discharge pipe 9, and the side edges of the conical top cover 12 are provided with two groups of exhaust pipes 11.
The two groups of exhaust pipes 11 are arranged side by side, the conical top cover 12 and the air inlet end of the air heater 10 are fixedly connected through the exhaust pipes 11 in a butt joint mode, and hot air exhausted from the drying tank 2 can be recovered by means of the arrangement of the exhaust pipes 11, so that the power consumption of the air heater 10 is reduced.
The inside of water conservancy diversion ring 3 is provided with annular gas pocket 16, and a plurality of groups of exhaust shower nozzles 14 are annular array in the inboard of water conservancy diversion ring 3, utilizes the setting of water conservancy diversion ring 3, and cooperation annular gas pocket 16 can form gas heating structure in the middle part of drying vessel 2, and when the glyphosate material of solution state passed drying vessel 2 middle part, can carry out the secondary heating to the glyphosate material of undried solution state for form the granular structure.
A connecting pipe 15 is fixedly arranged on the outer surface of one end of the guide ring 3, the guide ring 3 and the hot air pipe 8 are fixedly connected through the connecting pipe 15, and hot air exhausted by the hot air pipe 8 is led into the guide ring 3 by utilizing the arrangement of the connecting pipe 15 and is exhausted through an exhaust nozzle 14 of the guide ring 3.
One side of the drying tank 2 is provided with a raw material barrel 1, the upper end of the raw material barrel 1 is provided with a feed pipe 5, the upper end of the drying tank 2 is provided with a pump 6, the feed ends of the feed pipe 5 and the pump 6 are in butt joint and fixed, and glyphosate materials in solution in the raw material barrel 1 can be extracted through the feed pipe 5 by utilizing the pump 6.
The middle position of the outer surface of the upper end of the drying tank 2 is provided with a feeding groove 7, and the bottom of the conical top cover 12 is provided with a receiving bin 13.
In the centrifugal drying device for the production of the glyphosate, when the centrifugal drying device for the production of the glyphosate is used, an auxiliary drying structure is formed in the middle part of a drying tank 2, so that vaporific liquid is fully heated, the drying effect of the centrifugal drying device is improved, during operation, a user starts a pump 6, the pump 6 draws a raw material barrel 1 through a feed pipe 5, so that a glyphosate material in solution in the raw material barrel 1 is drawn out, the glyphosate material in solution is led into the centrifugal atomizer 4, the centrifugal atomizer 4 rotates at a high speed, the glyphosate material in solution is sprayed out in an atomized state, the user starts a hot air blower 10 in a way of electric heating, the hot air blower 10 is matched with a hot air pipe 8 to be led into the drying tank 2, the glyphosate material in the atomized state is quickly coagulated into a powdery solid structure after being heated in the drying tank 2, the arrangement of the guide ring 3 is utilized, and an annular air hole 16 is matched, so that a gas heating structure can be formed in the middle part of the raw material barrel 1, and when the glyphosate material in solution passes through the middle part of the drying tank 2, the glyphosate material in solution can be heated for a secondary drying structure, so that the granulated structure can be improved, and the glyphosate in the dried structure can be dried;
through setting up blast pipe 11, when this centrifugal drying device is used in glyphosate production, be linked together blast pipe 11 and the intake pipe of air heater 10 for air heater 10 has heat recovery structure, utilizes blast pipe 11's setting, can retrieve the interior exhaust steam of drying pot 2, thereby reduces the consumption of air heater 10, makes the heat that retrieves reintroduce into air heater 10, reduces this centrifugal drying device is used in glyphosate production's energy consumption, promotes its result of use.
The foregoing is merely illustrative of the structures of this utility model and various modifications, additions and substitutions for those skilled in the art can be made to the described embodiments without departing from the scope of the utility model or from the scope of the utility model as defined in the accompanying claims.
Claims (6)
1. The utility model provides a centrifugal drying device is used in glyphosate production, includes drying cylinder (2) and centrifugal atomizer (4), centrifugal atomizer (4) movable mounting is in the inside upper end position of drying cylinder (2), one side fixed mounting of drying cylinder (2) has air heater (10), link up through hot-blast main (8) between air heater (10) and drying cylinder (2), a serial communication port, the inboard middle part position of drying cylinder (2) is equipped with guide ring (3) that are used for carrying out auxiliary drying, the inboard fixed mounting of guide ring (3) has a plurality of groups exhaust shower nozzle (14), the exhaust end of exhaust shower nozzle (14) is the slope setting, the inboard lower part position of drying cylinder (2) is provided with toper top cap (12), the discharge end of toper top cap (12) and drying cylinder (2) is fixed through discharging pipe (9) butt joint, the side of toper top cap (12) is provided with two sets of blast pipe (11).
2. The centrifugal drying device for glyphosate production according to claim 1, wherein two groups of exhaust pipes (11) are arranged side by side, and the conical top cover (12) and the air inlet end of the hot air blower (10) are in butt joint and fixed through the exhaust pipes (11).
3. The centrifugal drying device for glyphosate production according to claim 1, wherein annular air holes (16) are formed in the guide ring (3), and a plurality of groups of exhaust spray heads (14) are arranged in an annular array on the inner side of the guide ring (3).
4. The centrifugal drying device for glyphosate production according to claim 1, wherein a connecting pipe (15) is fixedly arranged on the outer surface of one end of the guide ring (3), and the guide ring (3) and the hot air pipe (8) are in butt joint and fixed through the connecting pipe (15).
5. The centrifugal drying device for glyphosate production according to claim 1, wherein a raw material barrel (1) is arranged on one side of the drying tank (2), a feeding pipe (5) is arranged at the upper end of the raw material barrel (1), and a pump (6) is arranged at the upper end of the drying tank (2).
6. The centrifugal drying device for glyphosate production according to claim 5, wherein a feeding groove (7) is arranged in the middle of the outer surface of the upper end of the drying tank (2), and a receiving bin (13) is arranged at the bottom of the conical top cover (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321857298.9U CN220327935U (en) | 2023-07-14 | 2023-07-14 | Centrifugal drying device is used in glyphosate production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321857298.9U CN220327935U (en) | 2023-07-14 | 2023-07-14 | Centrifugal drying device is used in glyphosate production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220327935U true CN220327935U (en) | 2024-01-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321857298.9U Active CN220327935U (en) | 2023-07-14 | 2023-07-14 | Centrifugal drying device is used in glyphosate production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220327935U (en) |
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2023
- 2023-07-14 CN CN202321857298.9U patent/CN220327935U/en active Active
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