Efficient deoxidizing device

By designing a combination of multiple steam flow pipes and a deoxygenation circulating water tank, the problem of poor deoxygenation effect in dry quenching waste heat boilers was solved, achieving efficient deoxygenation and safe operation, reducing condensate risk, and improving the safety and reliability of the equipment.

CN224162579UActive Publication Date: 2026-04-24宁夏宝丰能源集团焦化二厂有限公司
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
宁夏宝丰能源集团焦化二厂有限公司
Filing Date
2025-05-26
Publication Date
2026-04-24

AI Technical Summary

Technical Problem

The existing deaerators of dry quenching waste heat boilers have poor deaeration effects when using different low-pressure steam, which cannot meet the dissolved oxygen requirements of high-temperature and high-pressure waste heat boilers, and there is also a safety hazard of condensate spraying from the deaerator exhaust port.

Method used

Design a high-efficiency deoxygenation device that achieves more comprehensive gas exchange through a combination of multiple steam flow pipes and a deoxygenation circulating water tank. Equipped with various safety valve interfaces and liquid level measuring instruments, it ensures equipment safety and deoxygenation efficiency.

Benefits of technology

It significantly improved the deoxygenation rate, reduced condensate at the deaerator exhaust port, prevented safety accidents, and enhanced the reliability and service life of the equipment.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model provides an efficient deoxidizing device, which comprises a deaerator and a deoxidizing circulating water tank communicated with the deaerator, the top of the deaerator is provided with a steam exhaust outlet pipeline, one side of the steam exhaust outlet pipeline is provided with a deaerator safety valve interface, the bottom of the deaerator is provided with a steam circulating port, and the steam circulating port is communicated with the deoxidizing circulating water tank. The other end of the steam circulation opening is connected into the deoxidizing circulation water tank, and a first steam circulation pipeline, a second steam circulation pipeline, a third steam circulation pipeline and a fourth steam circulation pipeline are arranged at the bottom of the deaerator and surround the steam circulation opening. One end of the first steam circulation pipeline and one end of the second steam circulation pipeline penetrate through the deoxidizing circulation water tank, and one end of the third steam circulation pipeline and one end of the fourth steam circulation pipeline are connected into the deoxidizing circulation water tank; the low-pressure steam can be effectively utilized, so that the dissolved oxygen meets the index requirement; condensate water at the exhaust port of the deaerator is greatly reduced, personal injury accidents are avoided, and the safety of workers is protected.
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Description

Technical Field

[0001] This utility model relates to a deoxygenation device, specifically, to a highly efficient deoxygenation device. Background Technology

[0002] The deoxygenated water required during the operation of dry quenching waste heat boilers is obtained through thermal and chemical deoxygenation. Thermal deaerators are designed with a heating steam pressure of 0.2 MPa. However, in practice, the low-pressure steam index used in different plants is not consistent, resulting in poor deoxygenation when using low-pressure steam for heating and deoxygenation. This fails to meet the dissolved oxygen requirement of less than 7 μg / L for high-temperature, high-pressure waste heat boilers. Furthermore, if the low-pressure steam pressure is too high, excessive condensate from the deaerator exhaust port can spray onto the ground, posing a safety hazard.

[0003] Therefore, there is an urgent need for a highly efficient deoxygenation device that can adapt to different low-pressure steam, effectively utilize low-pressure steam, and ensure that dissolved oxygen meets the required standards; the amount of condensate at the deaerator exhaust port should be significantly reduced to avoid personal injury accidents and protect the safety of workers. Summary of the Invention

[0004] Design a high-efficiency deoxygenation device that can effectively utilize low-pressure steam to ensure dissolved oxygen meets the required standards; significantly reduce condensate at the deaerator exhaust port to prevent personal injury accidents, protect worker safety, facilitate operation, reduce maintenance costs, and has wide applicability.

[0005] This utility model provides a highly efficient deoxygenation device, including a deaerator and a deoxygenation circulating water tank connected to the deaerator, wherein:

[0006] The deaerator is provided with a steam outlet pipe at the top, a deaerator safety valve interface on one side of the steam outlet pipe, a steam flow port at the bottom of the deaerator, and the other end of the steam flow port is connected to the deaerator circulating water tank. The bottom of the deaerator is provided with a first steam flow pipe, a second steam flow pipe, a third steam flow pipe and a fourth steam flow pipe around the steam flow port.

[0007] One end of the first steam flow pipe and the second steam flow pipe is connected to the deoxygenated circulating water tank, and one end of the third steam flow pipe and the fourth steam flow pipe is connected to the deoxygenated circulating water tank.

[0008] The first steam flow pipe and the second steam flow pipe pass through one end of the deaerator circulating water tank and are respectively connected to the low-pressure steam flow pipe. The other end of the low-pressure steam flow pipe is connected to the heating steam inlet. The heating steam inlet is connected to the public steam network. The bottom of the deaerator circulating water tank is provided with a deaerator outlet.

[0009] Preferably, the deaeration circulating water tank is provided with a water recirculation inlet, a secondary steam inlet, an auxiliary heating steam inlet, and a circulating water tank safety valve interface, and one end of the auxiliary heating steam inlet is connected to an auxiliary steam heating pipe.

[0010] Preferably, the deoxygenated circulating water tank is provided with several liquid level measuring instrument interfaces on one side.

[0011] Preferably, the deoxygenated circulating water tank is provided with several water supply pump balance water inlets on one side.

[0012] Preferably, a support platform is provided on one side of the deaerator, a guardrail is provided on the support platform, and a protective cage is provided on one side of the support platform.

[0013] Preferably, the first steam flow pipe, the second steam flow pipe, the third steam flow pipe and the fourth steam flow pipe are provided with openings on one side inside the deaerator.

[0014] Preferably, the deoxygenated circulating water tank has a drain outlet on one side of its bottom.

[0015] The beneficial effects of this utility model are as follows: This utility model provides a highly efficient deoxygenation device. Through the design of multiple steam flow pipes, it can achieve more comprehensive gas exchange and significantly improve the deoxygenation rate. It is equipped with multiple safety valve interfaces, which can effectively prevent safety accidents caused by excessive pressure, thus improving the safety of equipment use. The inclusion of a liquid level measuring instrument interface allows for real-time monitoring of the water level, making operation simpler and more intuitive, improving work efficiency, and enhancing the reliability and service life of the equipment. The optimized steam flow design reduces energy consumption. Attached Figure Description

[0016] Figure 1 This is a schematic diagram of a high-efficiency deoxygenation device according to the present invention.

[0017] Figure 2 This utility model relates to a highly efficient deoxygenation device. Figure 1 A partial schematic diagram;

[0018] Figure 3 This utility model relates to a highly efficient deoxygenation device. Figure 1 A partial schematic diagram of B;

[0019] Figure 4 This utility model relates to a highly efficient deoxygenation device. Figure 1 A top view of the steam inlet and the first, second, third, and fourth steam pipes of port A.

[0020] In the diagram: 1. Deaerator, 2. Exhaust outlet pipe, 3. Deaerator safety valve interface, 4. Protective cage, 5. Steam inlet, 6. Deaerator circulating water tank, 7. First steam flow pipe, 8. Second steam flow pipe, 9. Third steam flow pipe, 10. Fourth steam flow pipe, 11. Low-pressure steam flow pipe, 12. Heating steam inlet, 13. Deaerator outlet, 14. Feedwater recirculation inlet, 15. Liquid level measuring instrument interface, 16. Secondary steam inlet, 17. Auxiliary heating steam inlet, 18. Circulating water tank safety valve interface, 19. Auxiliary steam heating pipe, 20. Feedwater pump balance water inlet, 21. Support platform. Detailed Implementation

[0021] To make the technical solution of this utility model easier to understand, the technical solution of this utility model will now be clearly and completely described in conjunction with the accompanying drawings and specific embodiments.

[0022] Example 1:

[0023] like Figure 1-4 As shown, this embodiment of a high-efficiency deoxygenation device includes a deaerator 1 and a deoxygenation circulating water tank 6 connected to the deaerator 1, wherein:

[0024] The deaerator 1 is provided with a steam outlet pipe 2 at the top, and a deaerator safety valve interface 3 is provided on one side of the steam outlet pipe 2. The deaerator 1 is provided with a steam flow port 5 at the bottom, and the other end of the steam flow port 5 is connected to the deaerator circulating water tank 6. The bottom of the deaerator 1 is provided with a first steam flow pipe 7, a second steam flow pipe 8, a third steam flow pipe 9 and a fourth steam flow pipe 10 around the steam flow port 5.

[0025] One end of the first steam flow pipe 7 and the second steam flow pipe 8 is passed through the deoxygenated circulating water tank 6, and one end of the third steam flow pipe 9 and the fourth steam flow pipe 10 is connected to the deoxygenated circulating water tank 6.

[0026] The first steam flow pipe 7 and the second steam flow pipe 8 pass through one end of the deaerator circulating water tank 6 and are respectively connected to the low-pressure steam flow pipe 11. The other end of the low-pressure steam flow pipe 11 is connected to the heating steam inlet 12. The heating steam inlet 12 is connected to the public steam network. The bottom of the deaerator circulating water tank 6 is provided with a deaerator outlet 13.

[0027] The deoxygenated circulating water tank 6 is equipped with a water recirculation inlet 14, a secondary steam inlet 16, an auxiliary heating steam inlet 17, and a circulating water tank safety valve interface 18. One end of the auxiliary heating steam inlet 17 is connected to the auxiliary steam heating pipe 19.

[0028] The deoxygenated circulating water tank 6 is provided with several liquid level measuring instrument interfaces 15 on one side.

[0029] The deoxygenated circulating water tank 6 is equipped with several water supply pump balance water inlets 20 on one side.

[0030] The deaerator 1 is provided with a support platform 21 on one side, the support platform 21 is provided with a guardrail, and a protective cage 4 is provided on one side of the support platform 21.

[0031] The first steam flow pipe 7, the second steam flow pipe 8, the third steam flow pipe 9 and the fourth steam flow pipe 10 are provided with openings on one side inside the deaerator 1.

[0032] The deoxygenated circulating water tank 6 has a drain outlet on one side of its bottom.

[0033] When in use, the main material of deaerator 1 is highly corrosion resistant and can operate stably for a long time under high temperature and high pressure environments.

[0034] The first steam flow pipe 7 and the second steam flow pipe 8 can withstand high-pressure steam and are connected to the low-pressure steam flow pipe 11 to ensure smooth steam flow.

[0035] The third steam flow pipe 9 and the fourth steam flow pipe 10 also use the same inner diameter to enhance the overall deoxygenation effect.

[0036] The auxiliary heating steam inlet 17 is connected to the auxiliary steam heating pipe 19 to ensure that the water temperature is suitable and the deoxygenation efficiency is improved when the system is running in winter or under cooling conditions.

[0037] The exhaust outlet pipe 2 at the top of the deaerator and the deaerator safety valve interface 3 can release overpressure gas in a timely manner to ensure the safe operation of the equipment.

[0038] The deoxygenated circulating water tank 6 is equipped with multiple safety valve interfaces to reduce the risk of equipment damage.

[0039] Multiple liquid level measuring instrument interfaces 15 are installed on the side of the circulating water tank to ensure that operators can monitor the water level in real time and accurately control the water inlet and outlet.

[0040] Ensure that the equipment is installed correctly, all pipe connections are secure, and there are no leaks.

[0041] Water is injected into the circulating water tank 6 through the water recirculation inlet 14 to ensure that the water level reaches the set working level.

[0042] Open the heating steam inlet 12 until the desired temperature is reached.

[0043] Observe the liquid level measuring instrument interface 15 to ensure the water level is stable.

[0044] Under the action of steam heating, the water in the steam circulation pipes 7, 8 and 9, 10 comes into full contact with the steam, and the dissolved oxygen in the water is quickly removed.

[0045] During this period, monitor the pressure at deaerator outlet 13, drain outlet, and safety valve interface 3 to ensure that they are within the safe operating range.

[0046] If abnormal pressure is detected, it should be inspected and repaired promptly to prevent accidents.

[0047] Regularly drain the bottom sediment through the drain outlet.

[0048] The condensate inside the exhaust outlet pipe 2 will flow back into the deaerator along the exhaust outlet pipe 2.

[0049] It should be noted that the embodiments described herein are only some embodiments of this utility model, and not all implementations of this utility model. These embodiments are merely illustrative and are intended only to provide a more intuitive and clear way of understanding the content of this utility model, not to limit the technical solutions described herein. All other implementation methods that can be conceived by those skilled in the art without creative effort, as well as other simple substitutions and variations of the technical solutions of this utility model, without departing from the concept of this utility model, are within the protection scope of this utility model.

Claims

1. A highly efficient deoxygenation device, characterized in that, Includes a deaerator (1) and a deaerator circulating water tank (6) connected to the deaerator (1), wherein: The deaerator (1) is provided with a steam outlet pipe (2) at the top, and a deaerator safety valve interface (3) is provided on one side of the steam outlet pipe (2). The deaerator (1) is provided with a steam flow port (5) at the bottom, and the other end of the steam flow port (5) is connected to the deaerator circulating water tank (6). The bottom of the deaerator (1) is provided with a first steam flow pipe (7), a second steam flow pipe (8), a third steam flow pipe (9) and a fourth steam flow pipe (10) around the steam flow port (5). One end of the first steam flow pipe (7) and the second steam flow pipe (8) are both connected to the deoxygenated circulating water tank (6), and one end of the third steam flow pipe (9) and the fourth steam flow pipe (10) are connected to the deoxygenated circulating water tank (6). The first steam flow pipe (7) and the second steam flow pipe (8) pass through one end of the deaeration circulating water tank (6) and are respectively connected to the low-pressure steam flow pipe (11). The other end of the low-pressure steam flow pipe (11) is connected to the heating steam inlet (12). The heating steam inlet (12) is connected to the public steam network. The bottom of the deaeration circulating water tank (6) is provided with a deaerator outlet (13).

2. The high-efficiency deoxygenation device as described in claim 1, characterized in that, The deoxygenated circulating water tank (6) is provided with a water recirculation inlet (14), a secondary steam inlet (16), an auxiliary heating steam inlet (17) and a circulating water tank safety valve interface (18). One end of the auxiliary heating steam inlet (17) is connected to the auxiliary steam heating pipe (19).

3. The high-efficiency deoxygenation device as described in claim 1, characterized in that, The deoxygenated circulating water tank (6) is provided with several liquid level measuring instrument interfaces (15) on one side.

4. The high-efficiency deoxygenation device as described in claim 1, characterized in that, The deoxygenated circulating water tank (6) is provided with several water supply pump balance water inlets (20) on one side.

5. The high-efficiency deoxygenation device as described in claim 1, characterized in that, The deaerator (1) is provided with a support platform (21) on one side, and a guardrail is provided on the support platform (21). A cage (4) is provided on one side of the support platform (21).

6. The high-efficiency deoxygenation device as described in claim 1, characterized in that, The first steam flow pipe (7), the second steam flow pipe (8), the third steam flow pipe (9) and the fourth steam flow pipe (10) are provided with openings on one side inside the deaerator (1).

7. The high-efficiency deoxygenation device as described in claim 1, characterized in that, The deoxygenated circulating water tank (6) has a drain outlet on one side of its bottom.