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Changes in heat transfer performance of Inclined Double-Layer Tube Aluminum Tube Fin Evaporator under different working conditions

Publish Time: 2024-11-11
Inclined Double-Layer Tube Aluminum Tube Fin Evaporator plays a key role in many heat exchange applications, and its heat exchange performance will change significantly with different working conditions.

First of all, temperature conditions have a fundamental impact on heat transfer performance. In a low-temperature environment, for example, when the evaporator of a refrigeration system operates in low-temperature conditions, the temperature difference between the working fluid and the external environment increases. According to the principle of heat transfer, this will promote rapid heat transfer and accelerate the heat exchange rate. But at the same time, low temperature may cause changes in the physical properties of the working fluid, such as an increase in viscosity, which in turn will create resistance to the flow of fluid in the tube and weaken the heat transfer effect to a certain extent. Under high temperature conditions, the temperature difference is relatively reduced, the driving force for heat exchange becomes smaller, and the heat exchange rate may be reduced. However, high temperature may improve the fluidity of the working fluid. If this characteristic can be reasonably utilized to optimize the flow channel design, good heat exchange performance can be maintained to a certain extent.

Secondly, air flow rate is another important operating condition factor. When the air flow rate increases, the air passing over the surface of the fins can take away heat faster, strengthening the convection heat transfer process, and the heat transfer performance of the evaporator will be significantly improved. However, an excessively high air flow rate will increase the flow resistance on the air side, leading to an increase in fan power consumption, and may cause uneven airflow disturbance on the fin surface and differences in local heat exchange effects. On the contrary, if the air flow rate is too small, the heat accumulation speed on the fin surface may exceed the speed it is taken away, causing the evaporator surface temperature to decrease, and frost may even appear, seriously affecting the heat exchange efficiency.

Furthermore, changes in working fluid flow cannot be ignored. Increasing the working fluid flow can increase the convection heat transfer coefficient in the tube, allowing heat to be transferred within the tube more quickly. However, excessive working fluid flow will increase the power consumption of the pump, and may also cause the flow state of the working fluid in the tube to be unstable, such as excessive turbulence, which will affect the uniformity of heat transfer. If the working fluid flow rate is too small, the heat exchange area of the evaporator cannot be fully utilized, and the overall heat exchange efficiency is greatly reduced.

Finally, humidity conditions also have an impact on the heat transfer performance of the evaporator. In a high-humidity environment, moisture in the air easily condenses on the surface of the evaporator, forming a water film. On the one hand, the existence of the water film will increase the thermal resistance and reduce the heat exchange efficiency; on the other hand, if the temperature is further reduced, the water film may freeze, causing the evaporator to frost, which not only greatly hinders heat transfer, but also increases defrosting. energy consumption and time costs. In a low-humidity environment, although there is no problem of frost and condensation, because the physical properties such as the specific heat capacity of air are relatively stable, the room for improvement of heat exchange performance is relatively limited. Therefore, in practical applications, it is necessary to comprehensively consider various working conditions and conduct reasonable design, operation and maintenance of the Inclined Double-Layer Tube Aluminum Tube Fin Evaporator to achieve optimal heat exchange performance and energy utilization efficiency.
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