Steam conduction oil heat exchanger

By setting up a U-shaped heater tube bundle and insulation assembly in the steam heat transfer oil heat exchanger, the problem of underutilization of steam is solved, and efficient utilization of heat energy and reduction of gas costs are achieved.

CN223192133UActive Publication Date: 2025-08-05YULIN QINLUKE WASTE OIL TREATMENT CO LTD
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Patent Information

Application Number
CN202422024077.4
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-08-21
Publication Date
2025-08-05
Estimated Expiration
2034-08-21

AI Technical Summary

Technical Problem

In the prior art, the steam generated during the production process of hazardous waste lines is not fully utilized, resulting in waste of heat energy and increased gas costs, especially in the thermal oil furnace in the three-phase separation workshop, which is high in the cost of burning natural gas.

Method used

A steam heat conduction oil heat exchanger is designed. By setting up a U-shaped heater tube bundle and insulation assembly in the shell, the thermal conduction oil is heated by high-temperature steam, and the surface of the shell is heated through the insulation assembly to reduce heat loss and improve heat exchange efficiency.

Benefits of technology

The full utilization of steam has been achieved, the waste of steam produced by hazardous waste incineration lines and the gas costs of thermal oil furnaces have been reduced, and the heat exchange efficiency has been improved.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a steam conduction oil heat exchanger, which relates to the field of heat exchange, and comprises a shell, a tube plate and a sealing plate are arranged in the shell, the tube plate is matched with the sealing plate to form two independent cavities in the shell, a U-shaped heater tube bundle is arranged in the shell, and the U-shaped heater tube bundle is arranged in the shell. The two ends of the U-shaped heater tube bundle penetrate through the tube plate and correspond to the two cavities respectively. And a heat-conducting oil inlet and a heat-conducting oil outlet are respectively formed in the bottom and the top of the shell. The device has the beneficial effects that heat conduction oil flows in the U-shaped heater tube bundle, the U-shaped heater tube bundle is heated through high-temperature steam, the heat conduction oil is heated through the U-shaped heater tube bundle, part of steam input into the shell can be divided into the heat preservation assembly, and the surface of the shell can be heated through cooperation of the heat preservation assembly and the steam; therefore, the steam is fully utilized, the heat exchange efficiency is further improved, and the waste of steam produced by a hazardous waste incineration line and the gas cost of a heat conducting oil furnace are reduced.
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Description

Technical Field

[0001] The utility model relates to the technical field of heat exchange, in particular to a steam thermal oil heat exchanger. Background Art

[0002] During the production process of hazardous waste lines, the flue gas cooler is a set of equipment for cooling the flue gas. Generally, the steam generated in this process is discharged into the atmosphere through a muffler or condensed and recycled through a condenser.

[0003] The steam generated during the production process is basically discharged through the silencer and can only be used for heating and heat exchange in office buildings in winter. As the production line operates throughout the year, a large amount of steam is discharged, which invisibly wastes a lot of heat energy and is not fully utilized. It also wastes a lot of natural gas costs.

[0004] The three-phase separation workshop requires a large amount of heat source to heat the raw materials. The existing equipment for heating the raw materials in the three-phase separation workshop is a thermal oil furnace. Natural gas needs to be burned to heat the thermal oil, and then the thermal oil is used to exchange heat with the raw materials to reach the raw material production temperature. This process costs a lot of gas.

[0005] In order to make full use of the thermal energy of self-produced steam, reduce the waste of self-produced steam in the hazardous waste incineration line and the gas cost of the thermal oil furnace, we proposed a steam thermal oil heat exchanger. Utility Model Content

[0006] The purpose of the present invention is to provide a steam thermal oil heat exchanger in order to solve the above problems, as described below.

[0007] To achieve the above objectives, the present invention provides the following technical solutions:

[0008] The utility model provides a steam-heat-conducting oil heat exchanger, comprising a shell, a tube sheet and a sealing plate provided in the shell, the tube sheet and the sealing plate cooperating to form two independent cavities in the shell, a U-shaped heater tube bundle provided in the shell, and the two ends of the U-shaped heater tube bundle passing through the tube sheet and corresponding to the two cavities respectively;

[0009] The bottom and top of the shell are respectively provided with a heat transfer oil inlet and a heat transfer oil outlet, and the heat transfer oil inlet and the heat transfer oil outlet are respectively connected to the two cavities;

[0010] The shell is provided with a steam inlet and a drain outlet.

[0011] In the steam-heat-oil heat exchanger, the heat-conducting oil flows in the U-shaped heater tube bundle, and high-temperature steam is input into the shell through the steam inlet. The high-temperature steam heats the U-shaped heater tube bundle, and the heat-conducting oil is heated by the U-shaped heater tube bundle. Condensed water in the shell flows out through the drain port.

[0012] The steam input into the shell can be partially diverted to the insulation component. The insulation component and the steam can heat the shell surface and reduce the heat loss from the shell to the air, thereby fully utilizing the steam and improving the heat exchange efficiency.

[0013] Preferably, a heat-insulating component is provided on the surface of the shell, and the heat-insulating component is connected to the steam inlet, and the heat-insulating component can store steam.

[0014] Preferably, the insulation component includes a sleeve, which is sleeved on the surface of the shell, the surface of the shell is in contact with the inner wall of the sleeve, the interior of the sleeve is hollow, and a valve is provided on the sleeve, and the valve is connected to the steam inlet, and a pressure relief valve is provided at the bottom of the sleeve, and both the pressure relief valve and the valve are connected to the hollow part inside the sleeve.

[0015] Preferably, a plurality of partitions are provided in the hollow portion inside the sleeve, and through holes are provided on the partitions.

[0016] Preferably, a heat-insulating layer is provided on the surface of the sleeve.

[0017] Preferably, the end of the pressure relief valve is connected to a discharge pipe, and the end of the pressure relief valve corresponds to the inner wall of the discharge pipe.

[0018] Preferably, a plurality of reinforcement rings are provided on the surface of the shell.

[0019] Preferably, the bottom of the shell is provided with supporting feet, and the top of the shell is provided with lifting ears.

[0020] The beneficial effects are:

[0021] The heat transfer oil flows in the U-shaped heater tube bundle, and the U-shaped heater tube bundle is heated by high-temperature steam, and the heat transfer oil is heated by the U-shaped heater tube bundle. The steam input into the shell can be diverted to the insulation component. The insulation component and the steam cooperate to heat the shell surface, reducing the heat loss from the shell to the air, thereby achieving full utilization of the steam, further improving the heat exchange efficiency, and reducing the waste of self-produced steam in the hazardous waste incineration line and the gas cost of the thermal oil furnace. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the following briefly introduces the drawings required for use in the embodiments or the description of the prior art. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.

[0023] Figure 1This is a front view structural diagram of the utility model;

[0024] Figure 2 This is a schematic diagram of the front cross-sectional structure of the utility model;

[0025] Figure 3 This is a schematic diagram of the three-dimensional cross-sectional structure of the sleeve of the utility model;

[0026] Figure 4 It is a schematic diagram of the three-dimensional structure of the sleeve of the utility model.

[0027] The following are the descriptions of the reference numerals:

[0028] 1. Shell; 2. Support legs; 3. Lifting lugs; 4. Steam inlet; 5. Drain outlet; 6. Thermal oil inlet; 7. Thermal oil outlet; 8. Reinforcement ring; 9. Insulation assembly; 10. Valve; 11. Pressure relief valve; 12. Discharge pipe; 13. Sleeve; 14. Partition; 15. Through hole; 16. Insulation layer; 17. U-shaped heater tube bundle; 18. Tube sheet; 19. Sealing plate; 20. Cavity; 21. Support frame. DETAILED DESCRIPTION

[0029] To make the purpose, technical solution, and advantages of the present invention more clear, the technical solution of the present invention will be described in detail below. Obviously, the embodiments described are only some of the embodiments of the present invention, and not all of them. Based on the embodiments of the present invention, all other implementation methods obtained by ordinary technicians in this field without making any creative efforts are within the scope of protection of the present invention.

[0030] See also Figure 1-Figure 4 As shown, the utility model provides a steam-heat-conducting oil heat exchanger, comprising a shell 1, a tube sheet 18 and a sealing plate 19 provided in the shell 1, the tube sheet 18 and the sealing plate 19 cooperate to form two independent cavities 20 in the shell 1, a U-shaped heater tube bundle 17 is provided in the shell 1, and both ends of the U-shaped heater tube bundle 17 pass through the tube sheet 18 and correspond to the two cavities 20 respectively;

[0031] The bottom and top of the shell 1 are respectively provided with a heat transfer oil inlet 6 and a heat transfer oil outlet 7, and the heat transfer oil inlet 6 and the heat transfer oil outlet 7 are respectively connected to the two cavities 20;

[0032] The shell 1 is provided with a steam inlet 4 and a drain outlet 5 .

[0033] As an optional embodiment, a heat preservation component 9 is provided on the surface of the shell 1, and the heat preservation component 9 is connected to the steam inlet 4, and the heat preservation component 9 can store steam;

[0034] During actual use, after the steam enters the shell 1 , a portion of the steam is not utilized and is directly discharged through the drain port 5 , so part of the steam can be diverted to the heat preservation component 9 .

[0035] The heat preservation assembly 9 includes a sleeve 13, which is sleeved on the surface of the shell 1. The surface of the shell 1 is in contact with the inner wall of the sleeve 13. The interior of the sleeve 13 is hollow, and a valve 10 is provided on the sleeve 13. The valve 10 is connected to the steam inlet 4. A pressure relief valve 11 is provided at the bottom of the sleeve 13. Both the pressure relief valve 11 and the valve 10 are connected to the hollow part inside the sleeve 13.

[0036] After the steam enters the sleeve 13, it will not be discharged directly, but will be blocked by the pressure relief valve 11, thereby increasing the air pressure in the sleeve 13, thereby increasing the temperature of the sleeve 13. When the pressure in the sleeve 13 reaches the threshold, the pressure relief valve 11 automatically opens to relieve pressure.

[0037] A plurality of partitions 14 are provided in the hollow portion inside the sleeve 13 , and through holes 15 are provided on the partitions 14 . The partitions 14 are provided to reduce the flow velocity of steam in the sleeve 13 .

[0038] A thermal insulation layer 16 is provided on the surface of the sleeve 13 , and the thermal insulation layer 16 can reduce the heat flow rate of the sleeve 13 , thereby improving the thermal insulation effect of the thermal insulation component 9 .

[0039] The end of the pressure relief valve 11 is connected to a discharge pipe 12, and the end of the pressure relief valve 11 corresponds to the inner wall of the discharge pipe 12. The provision of the discharge pipe 12 can prevent the pressure relief valve 11 from spraying condensed water and gas by itself, and the pressure relief valve 11 is shielded by the discharge pipe 12 to ensure safety.

[0040] A plurality of reinforcement rings 8 are provided on the surface of the housing 1 , and the reinforcement rings 8 can improve the strength of the housing 1 .

[0041] The bottom of the shell 1 is provided with supporting feet 2, and the top of the shell 1 is provided with lifting ears 3.

[0042] With the above structure, the thermal oil flows in the U-shaped heater tube bundle 17, and the high-temperature steam is input into the shell 1 through the steam inlet 4. The high-temperature steam heats the U-shaped heater tube bundle 17, and the U-shaped heater tube bundle 17 heats the thermal oil. The condensed water in the shell 1 flows out through the drain port 5.

[0043] The steam input into the shell 1 can be partially diverted to the insulation component 9. The insulation component 9 cooperates with the steam to heat the surface of the shell 1, reducing the heat lost from the shell 1 to the air, thereby fully utilizing the steam and improving the heat exchange efficiency.

[0044] The above description is merely a specific embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any modifications or substitutions that can be easily conceived by a person skilled in the art within the technical scope disclosed in the present invention should be included within the scope of protection of the present invention. Therefore, the scope of protection of the present invention should be based on the scope of protection of the claims.

Claims

1. A steam thermal oil heat exchanger, characterized in that: The invention comprises a shell (1), wherein a tube sheet (18) and a sealing plate (19) are provided in the shell (1), wherein the tube sheet (18) and the sealing plate (19) cooperate to form two independent cavities (20) in the shell (1), and wherein a U-shaped heater tube bundle (17) is provided in the shell (1), and both ends of the U-shaped heater tube bundle (17) pass through the tube sheet (18) and correspond to the two cavities (20) respectively; The bottom and top of the shell (1) are respectively provided with a heat transfer oil inlet (6) and a heat transfer oil outlet (7), and the heat transfer oil inlet (6) and the heat transfer oil outlet (7) are respectively communicated with the two cavities (20); The shell (1) is provided with a steam inlet (4) and a drain outlet (5).

2. The steam thermal oil heat exchanger according to claim 1, characterized in that: A heat-insulating component (9) is provided on the surface of the shell (1), and the heat-insulating component (9) is in communication with the steam inlet (4), and the heat-insulating component (9) is capable of storing steam.

3. The steam-heat-conducting-oil heat exchanger according to claim 2, characterized in that: The heat preservation component (9) comprises a sleeve (13), the sleeve (13) is sleeved on the surface of the shell (1), the surface of the shell (1) is in contact with the inner wall of the sleeve (13), the interior of the sleeve (13) is hollow, and a valve (10) is provided on the sleeve (13), and the valve (10) is connected to the steam inlet (4), and a pressure relief valve (11) is provided at the bottom of the sleeve (13), and both the pressure relief valve (11) and the valve (10) are connected to the hollow part inside the sleeve (13).

4. The steam thermal oil heat exchanger according to claim 3, characterized in that: A plurality of partitions (14) are provided in the hollow portion inside the sleeve (13), and through holes (15) are provided on the partitions (14).

5. The steam thermal oil heat exchanger according to claim 3, characterized in that: A heat-insulating layer (16) is provided on the surface of the sleeve (13).

6. The steam thermal oil heat exchanger according to claim 3, characterized in that: The end of the pressure relief valve (11) is connected to a discharge pipe (12), and the end of the pressure relief valve (11) corresponds to the inner wall of the discharge pipe (12).

7. The steam thermal oil heat exchanger according to claim 1, characterized in that: A plurality of reinforcement rings (8) are provided on the surface of the shell (1).

8. The steam thermal oil heat exchanger according to claim 1, characterized in that: The bottom of the shell (1) is provided with a supporting foot (2), and the top of the shell (1) is provided with a lifting lug (3).