Low-energy-consumption purification device for ammonium perchlorate

By designing a low-energy-consumption purification device for ammonium perchlorate with a waste heat circulation mechanism, the problem of high energy consumption during heating in existing equipment has been solved, achieving energy reduction and environmental protection effects, and extending the equipment life.

CN224121749UActive Publication Date: 2026-04-14TIANYUAN (YICHANG) NEW MATERIAL TECH CO LTD
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-05-07
Publication Date
2026-04-14

AI Technical Summary

Technical Problem

Existing ammonium perchlorate purification equipment does not have a good waste heat recycling function during the heating process, resulting in high energy consumption and being detrimental to energy conservation and environmental protection.

Method used

Design a low-energy-consumption purification device for ammonium perchlorate that includes a waste heat recycling mechanism. The waste heat is recycled through components such as a condenser, coils, and water pumps, thereby reducing energy consumption and carbon emissions.

Benefits of technology

It significantly reduced energy consumption in the ammonium perchlorate purification process, reduced carbon emissions and energy costs, improved system thermal efficiency, extended equipment lifespan, and achieved the goals of energy conservation, emission reduction, and clean production.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a low-energy-consumption purification device for ammonium perchlorate, and relates to the technical field of inorganic salts. The ammonium perchlorate low-energy-consumption purification device comprises a device shell and a waste heat circulation mechanism, the waste heat circulation mechanism comprises a device bottom plate, a heating base, a condensation box, a coil pipe, a first gas outlet pipe and a second gas outlet pipe, the device bottom plate is fixedly connected to the bottom of the device shell, and the heating base is fixedly connected to the bottom of the device bottom plate; the condensing box is fixedly connected into the device shell, the bottom of the condensing box is fixedly connected with the device bottom plate, the coil pipe is fixedly connected to the outer surface of the condensing box, the multiple first air outlet pipes are fixedly connected to the surface of the condensing box, and each first air outlet pipe is fixedly connected with the coil pipe. Through the arrangement of the waste heat circulation mechanism, water vapor in the heating process heats the surface of the condensation box again, waste heat generated in the crystallization process is reused, the overall energy consumption can be remarkably reduced, and carbon emission and energy resources in the production process are reduced.
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Description

Technical Field

[0001] This utility model relates to the field of inorganic salt technology, and in particular to a low-energy-consumption purification device for ammonium perchlorate. Background Technology

[0002] Ammonium perchlorate is a white crystalline powder that is hygroscopic and readily soluble in water. It is a strong oxidizing agent and may explode when mixed with reducing agents, organic matter, or metal powders. Its main uses include being a key oxidizing agent for solid rocket propellants (widely used in spacecraft and missiles), as well as in the manufacture of explosives, pyrotechnics, and analytical reagents. When heated, this compound decomposes, releasing gases such as nitrogen, chlorine, oxygen, and water vapor. It must be stored in a cool, well-ventilated environment and protected from high temperatures, impacts, and contact with strong acids.

[0003] In the crystallization and purification process of ammonium perchlorate, purification equipment is required. The crude product is dissolved in hot water and concentrated to near saturation, and then slowly cooled to below 0°C to promote the preferential precipitation of ammonium perchlorate. However, the existing ammonium perchlorate purification equipment does not have a good waste heat circulation function when heating the crude product, resulting in higher energy consumption during heating, which is not conducive to energy conservation and environmental protection. Therefore, a low-energy consumption purification device for ammonium perchlorate is needed. Utility Model Content

[0004] The purpose of this utility model is to at least solve one of the technical problems existing in the prior art, and to provide a low-energy-consumption purification device for ammonium perchlorate, which can solve the problem that existing ammonium perchlorate purification equipment does not have a good waste heat circulation function when heating crude products, resulting in higher energy consumption during heating, which is not conducive to energy conservation and environmental protection.

[0005] To achieve the above objectives, this utility model provides the following technical solution: a low-energy-consumption purification device for ammonium perchlorate, comprising a device shell and a waste heat circulation mechanism. The waste heat circulation mechanism includes a device base plate, a heating base, a condenser, a coil, a first outlet pipe, and a second outlet pipe. The device base plate is fixedly connected to the bottom of the device shell, the heating base is fixedly connected to the bottom of the device base plate, the condenser is fixedly connected to the inside of the device shell, and the bottom of the condenser is fixedly connected to the device base plate. The coil is fixedly connected to the outer surface of the condenser. There are multiple first outlet pipes, all of which are fixedly connected to the surface of the condenser, and each first outlet pipe is fixedly connected to the coil. There are also multiple second outlet pipes, all of which are fixedly connected to the surface of the condenser, and each second outlet pipe is fixedly connected to the coil. The first outlet pipes are connected to the second outlet pipes through the coils, and the second outlet pipes extend to the outside of the device shell.

[0006] Preferably, the top of the condenser is fixedly connected to a liquid inlet, the inside of the condenser is fixedly connected to a condenser tube, the surface of the condenser tube is fixedly connected to multiple fins, the top of the condenser tube is fixedly connected to the liquid inlet, and the bottom of the condenser tube extends to the outside of the condenser and the outer shell of the device.

[0007] Preferably, a discharge pipe is fixedly connected to the bottom of the condensation box, a support rod is fixedly connected to the bottom of the heating base, and a fixed base is fixedly connected to the bottom of the support rod.

[0008] Preferably, a water tank is fixedly connected to the top of the fixed base, a water pump is fixedly connected to the top of the water tank, and a first water pipe is fixedly connected between the water tank and the water pump.

[0009] Preferably, a second water pipe is fixedly connected to the surface of the water pump, and an annular pipe is fixedly connected to the top of the condenser, with the second water pipe being fixedly connected to the annular pipe.

[0010] Preferably, a feeding pipe is fixedly connected to the top of the condensation box, and multiple nozzles are fixedly connected to the bottom of the annular pipe.

[0011] Compared with the prior art, the beneficial effects of this utility model are:

[0012] 1. This low-energy-consumption ammonium perchlorate purification device utilizes a waste heat circulation mechanism to reheat the surface of the condenser with water vapor generated during the heating process. This reuse of waste heat generated during crystallization significantly reduces overall energy consumption, carbon emissions, and energy costs during production. Simultaneously, it avoids environmental thermal pollution caused by direct emissions of high-temperature waste heat, improves system thermal efficiency, alleviates the load on the cooling system, and extends equipment lifespan. This achieves the dual goals of energy conservation, emission reduction, and clean production. It also solves the problem that existing ammonium perchlorate purification equipment lacks proper waste heat circulation when heating crude products, leading to higher energy consumption and hindering energy conservation and environmental protection. Attached Figure Description

[0013] The present invention will be further described below with reference to the accompanying drawings and embodiments:

[0014] Figure 1 This is a schematic diagram of the main body of this utility model;

[0015] Figure 2 This is a schematic diagram of the internal structure of this utility model;

[0016] Figure 3 This is a schematic diagram of the coil of this utility model;

[0017] Figure 4 For the present utility model Figure 3 Schematic diagram at point A in the middle.

[0018] Reference numerals in the attached drawings: 1. Device casing; 2. Device base plate; 3. Heating base; 4. Support rod; 5. Fixed base; 6. Water tank; 7. Water pump; 8. First water pipe; 9. Second water pipe; 10. Annular pipe; 11. Nozzle; 12. Liquid inlet; 13. Condenser pipe; 14. Fin; 15. Discharge pipe; 16. Condenser box; 17. Feeding pipe; 18. Coil; 19. First air outlet pipe; 20. Second air outlet pipe. Detailed Implementation

[0019] This section will describe in detail the specific embodiments of the present utility model. The preferred embodiments of the present utility model are shown in the accompanying drawings. The purpose of the drawings is to supplement the textual description with graphics, so that people can intuitively and vividly understand each technical feature and the overall technical solution of the present utility model, but they should not be construed as limiting the scope of protection of the present utility model.

[0020] In the description of this utility model, it should be understood that the directional descriptions, such as up, down, front, back, left, right, etc., indicate the directional or positional relationship based on the directional or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this utility model.

[0021] In the description of this utility model, terms such as greater than, less than, and exceeding are understood to exclude the stated number, while terms such as above, below, and within are understood to include the stated number. The use of "first" and "second" in the description is merely for distinguishing technical features and should not be construed as indicating or implying relative importance, or implicitly indicating the quantity or sequential relationship of the indicated technical features.

[0022] In the description of this utility model, unless otherwise explicitly defined, terms such as "setting," "installation," and "connection" should be interpreted broadly, and those skilled in the art can reasonably determine the specific meaning of the above terms in this utility model in conjunction with the specific content of the technical solution.

[0023] Please see Figure 1-4This utility model provides a technical solution: a low-energy-consumption purification device for ammonium perchlorate, including a device shell 1 and a waste heat circulation mechanism. The waste heat circulation mechanism includes a device base plate 2, a heating base 3, a condenser 16, a coil 18, a first outlet pipe 19, and a second outlet pipe 20. The device base plate 2 is fixedly connected to the bottom of the device shell 1, the heating base 3 is fixedly connected to the bottom of the device base plate 2, the condenser 16 is fixedly connected to the inside of the device shell 1, the bottom of the condenser 16 is fixedly connected to the device base plate 2, the coil 18 is fixedly connected to the outer surface of the condenser 16, there are multiple first outlet pipes 19, all of which are fixedly connected to the surface of the condenser 16, and each first outlet pipe 19 is fixedly connected to the coil 18. There are multiple second outlet pipes 20, all of which are fixedly connected to the surface of the condenser 16, and each second outlet pipe 20 is fixedly connected to the coil 18. The first outlet pipe 19 is connected to the second outlet pipe 20 through the coil 18, and the second outlet pipe 20 extends to the outside of the device shell 1.

[0024] Furthermore, a liquid inlet 12 is fixedly connected to the top of the condenser 16, a condenser tube 13 is fixedly connected inside the condenser 16, multiple fins 14 are fixedly connected to the surface of the condenser tube 13, the top of the condenser tube 13 is fixedly connected to the liquid inlet 12, the bottom of the condenser tube 13 extends to the outside of the condenser 16 and the outer shell 1 of the device, a discharge pipe 15 is fixedly connected to the bottom of the condenser 16, a support rod 4 is fixedly connected to the bottom of the heating base 3, a fixed base 5 is fixedly connected to the bottom of the support rod 4, a water tank 6 is fixedly connected to the top of the fixed base 5, a water pump 7 is fixedly connected to the top of the water tank 6, a first water pipe 8 is fixedly connected between the water tank 6 and the water pump 7, a second water pipe 9 is fixedly connected to the surface of the water pump 7, an annular pipe 10 is fixedly connected to the top of the condenser 16, the second water pipe 9 is fixedly connected to the annular pipe 10, a feeding pipe 17 is fixedly connected to the top of the condenser 16, and multiple nozzles 11 are fixedly connected to the bottom of the annular pipe 10.

[0025] Furthermore, raw materials are added to the interior of the condenser 16 through the feeding pipe 17, and the interior of the condenser 16 is heated by the heating base 3. Steam is discharged through the first vent pipe 19 and circulates inside the coil 18, and finally discharged through the second vent pipe 20, realizing the secondary utilization of waste heat. The coil 18 surrounds the outer surface of the condenser 16, which can ensure the utilization effect of waste heat. During crystallization, coolant is added to the interior of the condenser 13 through the liquid inlet 12 to cool the raw materials inside quickly. The cooling effect is better by setting multiple fins 14. After the device is used, the water pump 7 is started to introduce water into the annular pipe 10 and spray it out through multiple nozzles 11 to clean the interior of the condenser 13 and the condenser 16.

[0026] Furthermore, by setting up a waste heat circulation mechanism, the water vapor generated during the heating process can be used to reheat the surface of the condenser, thus reusing the waste heat generated during crystallization. This significantly reduces overall energy consumption, carbon emissions and energy costs during production, while avoiding environmental thermal pollution caused by the direct emission of high-temperature waste heat. It also improves system thermal efficiency, alleviates the load on the cooling system, and extends equipment lifespan, achieving the dual goals of energy conservation, consumption reduction, and clean production. This solves the problem that existing ammonium perchlorate purification equipment lacks a good waste heat circulation function when heating crude products, resulting in higher energy consumption during heating, which is detrimental to energy conservation and environmental protection.

[0027] Structural Description: Device Outer Shell 1: Serves as a protective shell for the entire device, preventing external impurities from entering;

[0028] Device base plate 2: It is fixed to the bottom of the device shell 1, supports the device shell 1 and the condenser box 16, and is fixed to the device shell 1 by high-strength bolts to ensure structural stability;

[0029] Heating base 3: It is fixed to the bottom of the device base plate 2 and directly contacts the bottom of the condensation box 16. It heats the material in the box evenly through heat conduction.

[0030] Support rod 4: Fixed to the bottom of heating base 3, used to connect heating base 3 and fixed base 5;

[0031] Fixed base 5: It is fixed to the bottom of the support rod 4 and provides support for the device;

[0032] Water tank 6: Fixed to the top of the fixed base 5, it stores cleaning water or cooling medium, and has a built-in water level sensor and filter screen;

[0033] Water pump 7: Fixed to the top of water tank 6, providing water circulation power, and transporting water to ring pipe 10 through first water pipe 8 and second water pipe 9;

[0034] Circular pipe 10: fixed to the top of the condenser box 16, evenly distributing water flow to the nozzle 11;

[0035] Nozzle 11: Fixed to the bottom of the annular tube 10. There are multiple nozzles 11. They clean the inner wall of the condenser tube 13 and the condenser box 16 to reduce scale buildup.

[0036] Liquid inlet 12: Fixed to the top of the condenser 16, it injects coolant (such as water or ethylene glycol solution) into the condenser tube 13;

[0037] Condenser 13: It is fixed inside the condenser box 16 and has a serpentine coil structure. It absorbs the heat of the material in the condenser box 16 through the circulation of coolant.

[0038] Fin 14: Aluminum fins are fixed to the surface of condenser tube 13 to increase the heat dissipation surface area and accelerate the crystallization process of ammonium perchlorate;

[0039] Discharge pipe 15: Fixed to the bottom of condenser 16, it discharges the purified ammonium perchlorate crystallization product, and is equipped with a pneumatic butterfly valve or ball valve at the bottom;

[0040] Condensation box 16: Fixed inside the outer shell 1 of the device, the core reaction vessel, containing ammonium perchlorate solution;

[0041] Feed pipe 17: It is fixed to the surface of the condenser 16 and feeds the raw material solution into the condenser 16. A sealing cover is provided on the top to prevent steam leakage.

[0042] Coil 18: It is fixed to the surface of the condenser 16 and wrapped around the outer surface of the condenser 16 to preheat subsequent materials using the waste heat of steam;

[0043] First exhaust pipe 19: fixed to the surface of condenser 16, guides the steam generated in condenser 16 to coil 18 for waste heat circulation.

[0044] The second exhaust pipe 20 is fixed to the surface of the coil 18, discharges the exhaust gas passing through the coil 18, and is connected to the exhaust gas treatment device at the end.

[0045] The embodiments of the present utility model have been described in detail above with reference to the accompanying drawings. However, the present utility model is not limited to the above embodiments. Within the scope of knowledge possessed by those skilled in the art, various changes can be made without departing from the spirit of the present utility model.

Claims

1. An ammonium perchlorate low energy purification apparatus, characterized by, include: Device casing (1); The waste heat circulation mechanism includes a device base plate (2), a heating base (3), a condenser (16), a coil (18), a first exhaust pipe (19), and a second exhaust pipe (20). The device base plate (2) is fixedly connected to the bottom of the device housing (1), the heating base (3) is fixedly connected to the bottom of the device base plate (2), the condenser (16) is fixedly connected to the inside of the device housing (1), and the bottom of the condenser (16) is fixedly connected to the device base plate (2). The coil (18) is fixedly connected to the condenser (19). 6) On the outer surface, there are multiple first vent pipes (19) and they are all fixedly connected to the surface of the condenser (16). Each first vent pipe (19) is fixedly connected to the coil (18). There are multiple second vent pipes (20) and they are all fixedly connected to the surface of the condenser (16). Each second vent pipe (20) is fixedly connected to the coil (18). The first vent pipe (19) is connected to the second vent pipe (20) through the coil (18). The second vent pipe (20) extends to the outside of the device housing (1).

2. The device for purifying ammonium perchlorate with low energy consumption according to claim 1, characterized in that: The top of the condenser (16) is fixedly connected to a liquid inlet (12), and the inside of the condenser (16) is fixedly connected to a condenser tube (13). Multiple fins (14) are fixedly connected to the surface of the condenser tube (13). The top of the condenser tube (13) is fixedly connected to the liquid inlet (12), and the bottom of the condenser tube (13) extends to the outside of the condenser (16) and the outer shell (1) of the device.

3. The device for purifying ammonium perchlorate with low energy consumption according to claim 1, characterized in that: The bottom of the condenser (16) is fixedly connected to the discharge pipe (15), the bottom of the heating base (3) is fixedly connected to the support rod (4), and the bottom of the support rod (4) is fixedly connected to the base (5).

4. The low-energy-consumption purification device for ammonium perchlorate according to claim 3, characterized in that: A water tank (6) is fixedly connected to the top of the fixed base (5), a water pump (7) is fixedly connected to the top of the water tank (6), and a first water pipe (8) is fixedly connected between the water tank (6) and the water pump (7).

5. The low-energy-consumption purification device for ammonium perchlorate according to claim 4, characterized in that: The surface of the water pump (7) is fixedly connected to a second water pipe (9), and the top of the condenser (16) is fixedly connected to an annular pipe (10). The second water pipe (9) and the annular pipe (10) are fixedly connected.

6. The low-energy-consumption purification device for ammonium perchlorate according to claim 1, characterized in that: The top of the condenser (16) is fixedly connected to a feeding pipe (17), and the bottom of the annular pipe (10) is fixedly connected to multiple nozzles (11).