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Heat-supply three-layer casing system based on countercurrent heat exchange principle

A bushing and principle technology, applied in heat exchange equipment, protecting pipelines and pipes through heat insulation, can solve the problems of large heat dissipation, heat waste, and large heat dissipation of heat pipes, so as to avoid waste, reduce losses, reduce Effect of small heat loss

Inactive Publication Date: 2011-10-26
XI AN JIAOTONG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Traditional heat transfer methods are mostly overhead pipelines or trench pipelines. The hot fluid pipeline and the return cold fluid pipeline are independent, only the outer walls of the respective pipelines are covered with insulation layers and exposed to the environment, but the temperature of the outer wall surface of the cold and hot pipeline insulation layer Still higher than the ambient temperature, the heat dissipation is relatively large, especially the heat dissipation of the heat pipe is greater, resulting in a lot of heat waste

Method used

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  • Heat-supply three-layer casing system based on countercurrent heat exchange principle
  • Heat-supply three-layer casing system based on countercurrent heat exchange principle
  • Heat-supply three-layer casing system based on countercurrent heat exchange principle

Examples

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example 1

[0028] Example 1: The thermal insulation material is asbestos wool, the thermal conductivity is 0.077W / (m K), the heating distance is 10,000 meters, the ambient temperature is 0°C, the steam temperature of the hot fluid outlet of the heating source section is 255.8°C, and the pressure is 4 ×10 -4 Pa, the mass flow rate is 10kg / s, and the outlet temperature of the cold fluid at the hot end is 130°C.

[0029] (1) If the traditional heat supply pipeline is used, the pipeline for conveying hot fluid and the pipeline for returning cold fluid are respectively set up, the outer diameter of the pipeline is 150mm, and the thickness of the insulation layer is 60mm. Let the inlet temperature of the thermal fluid at the hot end be t 1 , then the average temperature of the pipeline is In order to simplify the calculation, it is considered that the thermal resistance of the pipe wall is negligible compared with the insulation layer, and the average temperature of the pipe is used for cal...

example 2

[0074] Example 2: The insulation material is asbestos wool, the thermal conductivity is 0.077W / (m K), the heating distance is 10,000 meters, the ambient temperature is 0°C, the steam temperature of the hot fluid outlet of the heating source section is 255.8°C, and the pressure is 4 ×10 -4 Pa, the mass flow rate is 10kg / s, and the outlet temperature of the cold fluid at the hot end is 50°C.

[0075] (1) If the traditional heat transfer pipeline is used, the pipeline for conveying hot fluid and the pipeline for returning cold fluid are respectively set up, the outer diameter of the pipeline is 150mm, and the thickness of the insulation layer is 60mm. With the calculation method in Example 1, after multiple iterations, the inlet temperature t of the thermal fluid at the heat user end can be obtained 1 =221.3℃, the average temperature of the outer wall surface of the thermal fluid pipe insulation layer is t 2 =43.2℃, heat loss Φ 热 =1698897W.

[0076] In the same way, it can be...

example 3

[0078] Example 3: The insulation material is asbestos wool, the thermal conductivity is 0.077W / (m K), the heating distance is 10,000 meters, the ambient temperature is 20°C, the steam temperature of the hot fluid outlet of the heating source section is 255.8°C, and the pressure is 4 ×10 -4 Pa, the mass flow rate is 10kg / s, the outlet temperature of the cold fluid at the hot end is 130°C, and the pressure is 2.7×10 5 Pa.

[0079] (1) If the traditional heat transfer pipeline is used, the pipeline for conveying hot fluid and the pipeline for returning cold fluid are respectively set up, the outer diameter of the pipeline is 150mm, and the thickness of the insulation layer is 60mm. With the calculation method in Example 1, after multiple iterations, the inlet temperature t of the thermal fluid at the heat user end can be obtained 1 =225.7℃, the average temperature of the outer wall surface of the thermal fluid pipe insulation layer is t 2 =60.4℃, heat loss Φ 热 =1436699W. 269...

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Abstract

The invention provides a heat-supply three-layer casing system based on a countercurrent heat exchange principle. A thermal fluid flows through an inner pipe, a reflux cold fluid flows through an annular space between an inner pipe and an outer pipe, thermal insulating layers are wrapped on the outer walls of the inner and outer pipes, a layer of intermediate pipe is wrapped on the thermal insulating layer of the outer wall of the inner pipe so as to absorb the expansion of the inner pipe and the outer thermal insulating layer, and a certain gap is reserved between the intermediate pipe and the thermal insulating layer of the out wall of the inner pipe. The system provided by the invention can be used for overcoming the problems that the outer wall surfaces of the cold and heat pipes radiate heat to the surrounding medium in the traditional heat-supply process, the lost heat of the thermal fluid are all brought back by the cold fluid, and only the cold fluid radiates heat to the surrounding medium through the outer pipe; and the temperature gradient of the outer wall of a cold fluid pipe and the environment medium is smaller than that of the outer pipe wall of the thermal fluid and the environmental medium in the traditional mode, thus the heat dissipation with a larger temperature difference between a thermal fluid pipe wall and the environmental medium can be avoided and the heat-dissipating loss of a heat-supply pipeline can be greatly reduced.

Description

technical field [0001] The invention relates to a heat transfer and exchange device, in particular to a heat transfer three-layer casing system based on the principle of countercurrent heat exchange. Background technique [0002] In industrial and agricultural production and daily life, heating has a wide range of applications and is closely related to our production and life. Traditional heat transfer methods are mostly overhead pipelines or trench pipelines. The hot fluid pipeline and the return cold fluid pipeline are independent, only the outer walls of the respective pipelines are covered with insulation layers and exposed to the environment, but the temperature of the outer wall surface of the insulation layer of the hot and cold pipelines Still higher than the ambient temperature, the heat dissipation is larger, especially the heat dissipation of the heat pipe is larger, resulting in a large waste of heat. Contents of the invention [0003] The technical problem to...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F16L9/19F16L39/00F16L59/02
Inventor 吴东垠王利兵王健马晓骏
Owner XI AN JIAOTONG UNIV
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