The present invention relates generally to heat pipes, and more particularly to a heat pipe with a wick structure of screen mesh.
As electronic industry continues to advance, electronic components such as central processing units (CPUs), are made to provide faster operational speeds and greater functional capabilities. When a CPU operates at a high speed, its temperature frequently increases greatly. It is desirable to dissipate the heat generated by the CPU quickly.
To solve this problem of heat generated by the CPU, a cooling device is often used to be mounted on top of the CPU to dissipate heat generated thereby. It is well known that heat absorbed by fluid having a phase change is ten times more than that the fluid does not have a phase change; thus, the heat transfer efficiency by phase change of fluid is better than other mechanisms, such as heat conduction or heat convection. Accordingly, a heat pipe has been developed.
The heat pipe has a hollow pipe body receiving a working fluid therein and a wick structure disposed on an inner wall of the pipe body. Generally the heat pipe is divided into an evaporating section, an adiabatic section and a condensing section along a longitudinal direction thereof. During operation of the heat pipe, the working fluid absorbs the heat generated by the CPU or other electronic device and evaporates into vapor. The vapor moves from the evaporating section to the condensing section to dissipate the heat, whereby the vapor cools and condenses at the condensing section. The condensed working fluid returns to the evaporating section via a capillary force generated by the wick structure. From the evaporating section, the fluid is evaporated again to thereby repeat the heat transfer from the evaporating section to the condensing section.
In general, movement of the working fluid depends on the capillary pressure (force) of the wick structure. Usually the wick structure has following four configurations: sintered powders, grooves, fiber and screen mesh. Since the thickness and pore size of the screen mesh can be easily changed, the screen mesh is widely used in the heat pipe.
It is well recognized that the capillary pressure of a screen mesh increases due to a decrease in the pore size of the screen mesh. In order to obtain a relatively large capillary pressure, a mesh screen having a small-sized pore is usually adopted. However, it is not always the best way to choose a screen mesh having small-sized pores, because the flow resistance to the condensed working fluid also increases due to a decrease in the pore size of the screen mesh. The increased flow resistance reduces the speed of the condensed working fluid in returning back to the evaporating section and therefore limits the heat transfer performance of the heat pipe. As a result, a heat pipe with a screen mesh that has too large or too small a pore size often suffers dry-out problem at the evaporating section as the condensed working fluid cannot be timely sent back to the evaporating section of the heat pipe.
Therefore, there is a need for a heat pipe with a screen mesh which can provide simultaneously a relatively large capillary pressure and a relatively low flow resistance so as to effectively and timely bring the condensed working fluid back from the condensing section to the evaporating section of the heat pipe and thereby to avoid the undesirable dry-out problem at the evaporating section.
According to a preferred embodiment of the present invention, a heat pipe comprises a hollow pipe body for receiving a working fluid therein and a screen mesh disposed in the pipe body. The screen mesh comprises at least two layers. One of the two layers is in the form of a planar layer and the other of the two layers is in the form of a wave layer. The wave layer forms a plurality of flowing channels for the working fluid to flow from a condensing section to an evaporating section of the heat pipe. The channels formed by the wave layer of the screen mesh is capable of reducing the flow resistance to the condensed fluid to flow back while pores in the screen mesh are capable of providing a relatively large capillary pressure for drawing the condensed fluid to flow back.
Other advantages and novel features of the present invention will be drawn from the following detailed description of a preferred embodiment of the present invention with attached drawings, in which:
Referring to
The pipe body 20 is made of high heat conductivity material such as copper or copper alloys. The screen mesh 30 has a plurality of pores and is saturated with a working fluid (not shown). The working fluid may be water, alcohol or other material having a low boiling point; thus, the working fluid can easily evaporate to vapor during operation when the evaporating section receives heat from a heat-generating electronic device, such as a CPU.
The screen mesh 30 comprises a wave layer 40 and a planar layer 50 arranged along circumferential and axial directions of the pipe body 20. The wave layer 40 is staked on the inner wall 22 of the pipe body 20 while the planar layer 50 is stacked on the wave layer 40 along a radial direction of the heat pipe 10 from a center to a periphery thereof. The wave layer 40 is directly attached to the inner wall 22 of the pipe body 20. The planar layer 50 is disposed on an inner side of the wave layer 40.
As best seen in
During operation of the heat pipe 10, when the working fluid saturated in the screen mesh 30 at the evaporating section of the heat pipe 10 evaporates to vapor due to heat absorbed from the CPU, the vapor moves toward the condensing section of the heat pipe 10 due to the difference of vapor pressure to perform heat transport. The vapor then cools and condenses at the condensing section to perform heat dissipation. In this case, the condensed working fluid is absorbed into the screen mesh 30 at the condensing section, and then returns to the evaporating section through the screen mesh 30. The pores of the screen mesh 30 can provide a relatively large capillary pressure to the working fluid while the flow channels 48 can provide a relatively small flow resistance to the working fluid. The screen mesh 30 accordingly can increase the speed of the condensed working fluid in returning back to the evaporating section and therefore promotes the heat transfer performance of the heat pipe 10. As a result, a dry-out problem of the heat pipe 10 can be avoided.
Referring to
It is to be understood that the screen mesh 30, 430, 630 is used to provide capillary pressure to force the working fluid returning back to the evaporating section. The screen mesh 30, 430, 630 may be in the form of a multi-layer structure more than two layers. Referring to
It is understood that the invention may be embodied in other forms without departing from the spirit thereof. Thus, the present example and embodiment is to be considered in all respects as illustrative and not restrictive, and the invention is not to be limited to the details given herein.
Number | Date | Country | Kind |
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094102615 | Jan 2005 | TW | national |