Incinerator recovered heat energy preheating system

By designing a preheating system for heat recovery of incinerators and using the combination of heat exchanger and S water pipes, the problem that incinerators cannot effectively recover and reuse heat is solved, and the effect of heat recovery and energy saving is achieved.

CN222688203UActive Publication Date: 2025-03-28SANJIANG CHEM CO LTD
View PDF 0 Cites 0 Cited by

Patent Information

Application Number
CN202420339307.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-02-23
Publication Date
2025-03-28
Estimated Expiration
2034-02-23

AI Technical Summary

Technical Problem

Existing incinerators cannot effectively recycle and reuse heat from furnace temperature and boiler outer wall temperature, resulting in increased energy consumption and increased production and operation costs.

Method used

A preheating system for thermal energy recovery of incinerators is designed, including furnace body, feed port, gas pipe, filter, air flow pipe, heat exchanger and S water pipe. Through the combination of the heat exchanger and the S water pipe, the filtered gas enters the S water pipe through the gas flow pipe. The heat absorption ring adsorbs the heated gas and the fluid to be heated, and releases the heat absorbed heat and transfers it to the fluid to be heated to achieve preheating.

Benefits of technology

Through thermal energy recovery and reuse, the use of steam heat sources is reduced, energy is saved, and production and operation costs are reduced.

✦ Generated by Eureka AI based on patent content.

Smart Images

  • Figure CN222688203U_ABST
    Figure CN222688203U_ABST
Patent Text Reader

Abstract

The utility model belongs to the technical field of energy conversion, and particularly relates to an incinerator recovered heat energy preheating system which comprises an incinerator body, the upper surface of the incinerator body is fixedly sleeved with a feeding port and a gas pipe respectively, one end of the gas pipe is fixedly sleeved with an inlet of a filter, the upper surface of the filter is fixedly sleeved with an airflow pipe, and the airflow pipe is fixedly sleeved with an air outlet of the filter. And one end of the airflow pipe is fixedly sleeved with a heat exchanger. According to the incinerator recovered heat energy preheating system, by arranging the heat exchanger, gas with dust filtered out enters the S-shaped water pipe through the airflow pipe, the heat absorption ring in the S-shaped water pipe adsorbs heated gas and fluid to be heated, heat absorbed by heat is released and transmitted to the fluid to be heated, and preheating is achieved; heat of gas in the S-shaped water pipe can be transmitted to fluid entering the heat exchanger through the cold inlet, the fluid transmits the heat to a heat load, and heat energy is recycled and reused in the process.
Need to check novelty before this filing date? Find Prior Art

Description

Technical Field

[0001] The utility model relates to the technical field of energy conversion, in particular to a preheating system for recovering heat energy from an incinerator. Background Art

[0002] The incinerator is mainly used for harmless treatment of various waste gases generated during the production of the device, especially gases harmful to the environment. After incineration, it can produce 340 tons of 13MPa steam / 24 hours. The operation of the equipment is directly related to the safety and environmental protection of the entire device. It is a key equipment unit. The incinerator mainly accepts the waste gas from the device for high-temperature treatment. When the waste gas is sufficient, the gas pipeline network will add a small amount of auxiliary fuel gas to make the incineration more complete and 100% meet the emission standards. When the device is shut down or the waste gas is insufficient, the fuel gas pipeline network will serve as a supplement to keep the torch lit.

[0003] However, the existing incinerator maintains a furnace temperature of 1100°C all year round, and the boiler outer wall temperature is maintained at around 120°C all year round. The heat of the main body cannot be recovered, nor can the desalted water be preheated by heat. The use of steam heat source is increased, thereby consuming more energy and increasing production and operation costs. Utility Model Content

[0004] Based on the existing technical problems, the utility model proposes an incinerator heat recovery preheating system.

[0005] The utility model proposes an incinerator heat recovery preheating system, comprising a furnace body, the upper surface of which is respectively fixedly sleeved with a feed port and a gas pipe, one end of the gas pipe is fixedly sleeved with the inlet of a filter, and the upper surface of the filter is fixedly sleeved with an airflow pipe.

[0006] Preferably, a heat exchanger is fixedly sleeved on one end of the airflow tube, a device cover is movably connected to the upper surface of the heat exchanger, and the upper surface of the device cover is fixedly sleeved on one end of the airflow tube through an airflow port.

[0007] Preferably, the peripheral side of the device cover is fixedly mounted with symmetrically distributed buckles, the upper peripheral side of the heat exchanger is provided with a square groove, the inner wall of the square groove is movably engaged with one side surface of the buckle, and the peripheral side of the heat exchanger is respectively provided with a cold inlet, a cold outlet and a discharge port.

[0008] Preferably, an S-shaped water pipe is movably connected to the inner wall of the heat exchanger, a circular groove is provided on the inner wall of the S-shaped water pipe, and heat-absorbing rings evenly distributed are fixedly installed in the circular groove.

[0009] Preferably, a threaded groove is provided on the outer surface of the transversely distributed node pipe of the S water pipe, a heat-conducting strip is fixedly installed on the inner wall of the threaded groove, the material of the heat-conducting strip is alumina, and a heat-dissipating block with a fan-shaped structure is fixedly connected to the peripheral surface of the heat-conducting strip, the material of the heat-dissipating block is graphite.

[0010] Preferably, one end of the air flow pipe is fixedly sleeved with one end of the S water pipe, and one end of the S water pipe is fixedly connected with one end of the discharge port.

[0011] The beneficial effects of the present invention are:

[0012] By setting up the heat exchanger, the gas after filtering out dust enters the S water pipe through the air flow pipe. The heat-absorbing ring in the S water pipe adsorbs the heated gas and the fluid to be heated, and releases the absorbed heat to transfer to the fluid to be heated to achieve preheating. The heat of the gas in the S water pipe will be transferred to the fluid entering the heat exchanger through the cold inlet, and the fluid transfers the heat to the heat load. In this process, heat energy is recovered and reused, and the recovered heat is used to preheat the desalted water, thereby reducing the use of steam heat source, and ultimately achieving the purpose of saving energy and reducing production and operation costs. BRIEF DESCRIPTION OF THE DRAWINGS

[0013] Figure 1 This is a schematic diagram of a preheating system for recovering heat energy from an incinerator proposed by the utility model;

[0014] Figure 2 A three-dimensional diagram of the heat exchanger structure of an incinerator heat recovery preheating system proposed by the utility model;

[0015] Figure 3 A three-dimensional diagram of the S water pipe structure of an incinerator heat recovery preheating system proposed by the utility model;

[0016] Figure 4 This is a three-dimensional diagram of the heat-conducting strip structure of an incinerator heat recovery preheating system proposed by the utility model.

[0017] In the figure: 1. furnace body; 2. feed inlet; 3. gas pipe; 4. filter; 5. air flow pipe; 6. heat sink; 7. heat exchanger; 8. cover; 9. buckle; 10. cold inlet; 11. cold outlet; 12. discharge port; 13. S water pipe; 14. round groove; 15. heat absorption ring; 16. threaded groove; 17. heat conduction strip. DETAILED DESCRIPTION

[0018] The technical solutions in the embodiments of the present invention will be described clearly and completely below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all of the embodiments.

[0019] Reference Figure 1-Figure 4 A heat recovery preheating system for an incinerator comprises a furnace body 1, the upper surface of which is fixedly sleeved with a feed port 2 and a gas pipe 3, one end of the gas pipe 3 is fixedly sleeved with the inlet of a filter 4, and the upper surface of the filter 4 is fixedly sleeved with an airflow pipe 5.

[0020] One end of the airflow tube 5 is fixedly connected with a heat exchanger 7, and the upper surface of the heat exchanger 7 is movably connected with a device cover 8. The upper surface of the device cover 8 is fixedly connected with one end of the airflow tube 5 through the airflow port to determine the position of the device cover 8, and the filtered gas enters the heat exchanger 7 through the airflow tube 5.

[0021] The circumferential side of the cover 8 is fixedly mounted with symmetrically distributed buckles 9, the circumferential side of the upper end of the heat exchanger 7 is provided with a square groove, the inner wall of the square groove is movably engaged with the surface of one side of the buckle 9, and the circumferential side of the heat exchanger 7 is respectively provided with a cold inlet 10, a cold outlet 11 and a discharge port 12. The design of the square groove and the buckle 9 allows the cover 8 to be stuck and fixed, and can also be removed for easy cleaning of the inside of the heat exchanger 7.

[0022] The inner wall of the heat exchanger 7 is movably connected with an S water pipe 13, and the inner wall of the S water pipe 13 is provided with a circular groove 14. The circular groove 14 is fixedly installed with evenly distributed heat absorbing rings 15. The position of the circular groove 14 is determined, and the heat absorbing ring 15 in the circular groove 14 can heat the gas in the S water pipe 13.

[0023] A thread groove 16 is provided on the outer surface of the transversely distributed section of the S water pipe 13, and a heat conducting strip 17 is fixedly installed on the inner wall of the thread groove 16. The material of the heat conducting strip 17 is alumina. The peripheral surface of the heat conducting strip 17 is fixedly connected with a heat sink 6 with a fan-shaped structure. The material of the heat sink 6 is graphite. The setting of the thread groove 16 enables the heat conducting strip 17 in the thread groove 16 to evenly distribute heat to the gas in the S water pipe 13, avoiding the generation of hot spots or cold spots and improving the accuracy of temperature control. The heat sink 6 on the heat conducting strip 17 can help reduce the temperature and evenly distribute the heat.

[0024] One end of the airflow tube 5 is fixedly connected to one end of the S water pipe 13, and one end of the S water pipe 13 is fixedly connected to one end of the discharge port 12 to determine the position of the discharge port 12. The gas enters the S water pipe 13 through the airflow tube 5 and is finally discharged from the discharge port 12.

[0025] By setting up the heat exchanger 7, the gas after filtering out dust enters the S water pipe 13 through the airflow pipe 5. The heat absorption ring 15 in the S water pipe 13 adsorbs the heated gas and the fluid to be heated, releases the absorbed heat and transfers it to the fluid to be heated to achieve preheating. The heat of the gas in the S water pipe 13 will be transferred to the fluid entering the heat exchanger 7 through the cold inlet 10, and the fluid transfers the heat to the heat load. In this process, heat energy is recovered and reused, and the recovered heat is used to preheat the desalted water, thereby reducing the use of steam heat source, and ultimately achieving the purpose of saving energy and reducing production and operation costs.

[0026] Working principle: Pour the material into the feed port 2 and burn it in the incinerator. The combustion exhaust gas flows into the filter 4 through the gas pipe 3. The filtered gas flows into the S water pipe 13 in the heat exchanger 7 through the air flow pipe 5. The heat absorption ring 15 in the S water pipe 13 adsorbs the heated gas and the fluid to be heated, and releases the absorbed heat to transfer to the fluid to be heated to achieve preheating.

[0027] The heat of the gas in the S water pipe 13 will be transferred to the fluid entering the heat exchanger 7 through the cold inlet 10. The process of heat transfer between the two fluids can recover and reuse the heat energy. The materials used for the heat conducting strips 17 and the heat dissipating blocks 6 are corrosion-resistant and have better heat conduction and heat dissipation, which plays a role in uniform heat distribution, thereby reducing the use of steam heat source, and ultimately achieving the purpose of saving energy and reducing production and operation costs. At the same time, the cover 8 on the heat exchanger 7 can be removed to clean the inside of the heat exchanger.

[0028] The above description is only a preferred specific implementation manner of the present invention, but the protection scope of the present invention is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes within the technical scope disclosed by the present invention according to the technical scheme and the utility model concept of the present invention, which should be covered by the protection scope of the present invention.

Claims

1. An incinerator heat recovery preheating system, comprising a furnace body (1), characterized in that: The upper surface of the furnace body (1) is respectively fixedly sleeved with a feed port (2) and a gas pipe (3); one end of the gas pipe (3) is fixedly sleeved with the inlet of the filter (4); and the upper surface of the filter (4) is fixedly sleeved with an airflow pipe (5); One end of the airflow tube (5) is fixedly sleeved with a heat exchanger (7), the upper surface of the heat exchanger (7) is movably connected with a device cover (8), the upper surface of the device cover (8) is fixedly sleeved with one end of the airflow tube (5) through an airflow port, the inner wall of the heat exchanger (7) is movably connected with an S water pipe (13), the inner wall of the S water pipe (13) is provided with a circular groove (14), and heat absorbing rings (15) are fixedly installed in the circular groove (14) in a uniformly distributed manner.

2. The incinerator heat recovery preheating system according to claim 1 is characterized in that: The peripheral side surface of the device cover (8) is fixedly mounted with symmetrically distributed buckles (9), the upper peripheral side surface of the heat exchanger (7) is provided with a square groove, the inner wall of the square groove is movably engaged with a side surface of the buckle (9), and the peripheral side surface of the heat exchanger (7) is respectively provided with a cold inlet (10), a cold outlet (11) and a discharge port (12).

3. The incinerator heat recovery preheating system according to claim 2 is characterized in that: The outer surface of the transversely distributed section of the S water pipe (13) is provided with a threaded groove (16), the inner wall of the threaded groove (16) is fixedly mounted with a heat conducting strip (17), the material of the heat conducting strip (17) is aluminum oxide, and the peripheral surface of the heat conducting strip (17) is fixedly connected with a heat dissipation block (6) in a fan-shaped structure, the material of the heat dissipation block (6) is graphite.

4. The incinerator heat recovery preheating system according to claim 3 is characterized in that: One end of the air flow pipe (5) is fixedly sleeved with one end of the S water pipe (13), and one end of the S water pipe (13) is fixedly connected with one end of the discharge port (12).