This invention deals generally with loop heat pipe evaporators, and more specifically with increasing the heat transfer from the location of heat input to the evaporator.
One of the limitations for loop heat pipes is related to the heat input to the evaporator. Conventional loop heat pipe primary wicks have a heat flux limit at approximately 25 W/cm2. Excessive heat flux causes boiling inside the wick, which disrupts liquid return flow and results in unstable operation of the loop heat pipe and dry-out.
The maximum heat flux in the evaporator wick and typically in the entire loop heat pipe system is found at the interface between the wick and evaporator casing. At this location, heat transfer can occur by two paths, by conduction through the liquid—saturated wick or by convection of the vapor in the vapor grooves that are along the casing inner surfaces and/or the wick outer surfaces. To transfer heat by convection the vapor must collect the heat from the evaporator casing and then deposit this heat in the wick. This is a poor heat transfer path because of the relatively low convective heat transfer coefficient of the vapor flow. Conduction requires heat to move from the location of heat input through the evaporator casing directly to the liquid-saturated wick and is a much more favorable method. However, the vapor grooves are located between the wick and evaporator casing. As a result, they reduce the heat transfer area available for conduction. This reduction in area concentrates heat flux, and as a result the highest heat flux occurs at this point. This problem is aggravated by non-uniform heat flux distribution, which further concentrates the heat flux. To increase the heat flux tolerated at the heat input location of the loop heat pipe, this heat flux concentration needs to be reduced.
Therefore the purpose of the present invention is to produce a more uniform heat flux at the interface between the loop heat pipe wick and evaporator casing.
The present invention is an evaporator for a loop heat pipe with improved input heat transfer. The improved heat transfer is attained by constructing an independent heat pipe on the entire evaporator heat input surface. The heat pipe then distributes the heat from the limited heat input areas to the entire surface of the loop heat pipe evaporator, and the entire evaporator surface functions in the loop heat pipe as opposed to the limited smaller areas into which the heat usually enters.
Prior art loop heat pipe evaporators typically have cylindrical casings with porous wick on the inside surface of the cylinder and axially oriented grooves where the porous wick meets the cylinder inside wall. The present invention adds an annular heat pipe as a thermal spreader in good thermal contact with the outer surface of the evaporator casing. Such a heat pipe can be constructed so that it uses the evaporator casing wall as one side of the heat pipe or as an independent structure bonded to the outer wall of the evaporator casing.
In either type of structure, the heat pipe outer wall acts as the heat input surface, and the heat pipe wick on the inside of the heat pipe outer wall at the heat input area produces vapor that travels throughout the entire heat pipe and condenses in near uniform fashion on the entire inside surface of the heat pipe that is in contact with the evaporator of the loop heat pipe. Thus, the heat from the limited heat input area of the heat pipe is transferred to the entire loop heat pipe evaporator heat input surface with very little thermal resistance.
Simply stated, the added heat pipe of the present invention spreads the heat so that the effect is the same as if the heat entering the loop heat pipe evaporator had been uniformly applied over the entire loop heat pipe evaporator surface rather than a very limited area. Since, as previously noted, conventional loop heat pipe wicks have a heat flux limit of approximately 25 W/cm2 and heat pipe wick structures have heat flux limits in the range of 75-500 W/cm2, the heat pipe accepts the higher heat input with much higher heat flux capability, and its heat spreading action increases the affected input heat surface area of the loop heat pipe evaporator so that it has no problem accepting the greater total heat input.
As shown in both figures, heat pipe 12 is attached to casing wall 14 of evaporator 10, and is constructed so that it uses evaporator casing wall 14 as one wall of heat pipe 12. However, heat pipe 12 can also be constructed as a separate structure which is bonded to casing wall 14 of evaporator 10. It should also be appreciated that although in
Loop heat pipe evaporator 10 is shown with the conventional structure of such an evaporator. Prior art loop heat pipe evaporators typically have cylindrical casings 14 with capillary wick 16 on the inside surface of the cylinder and axially oriented grooves 18 (
Except for its annular structure, heat pipe 12 also has a reasonably conventional structure for a heat pipe. It includes evaporator wick 20 on the interior surface 19 of a first pipe or casing wall 22 and condenser wick 21 on the interior surface 25 of a second pipe or casing wall 23, with vapor space 24 between wicks 20 and 21.
However, additional wick structures are needed in heat pipe 12 because of its annular configuration. Since evaporator wick 20 and condenser wick 21 basically are isolated concentric cylinders, they have no capillary path between them to return condensed liquid from condenser wick 21 back to evaporator wick 20 for continuing operation, except with the addition bridge wicks 26 as shown in
The operation of the invention is straight forward. Heat input in even such a limited access as location A is actually applied to exterior wall 22 of annular heat pipe 12 where it evaporates liquid from evaporator wick 20. Then, as is conventional for heat pipe operation, the vapor resulting from the evaporation moves throughout heat pipe vapor space 24, and when it contacts the cooler condenser wick 21 on heat pipe casing inner wall 23, the vapor condenses transferring the input heat to heat pipe casing inner wall 23. The input heat has thereby been transferred from the very limited area at heat input location A to the entire casing wall 14 of evaporator 10 with virtually no heat loss because of the operation of heat pipe 12. This heat spreading action thereby increases the affected input heat surface area of the loop heat pipe evaporator so that it has no problem accepting a much greater total heat input.
It should be appreciated that while in the preferred embodiment shown heat pipe inner wall 23 also functions as the heat input wall of loop heat pipe evaporator 10, essentially this same structure could be constructed as an independent annular heat pipe structure with its inner wall bonded to the outer wall of the evaporator casing. The only difference being that wall 23 would be constructed of two walls bonded together rather than a single integrated wall as shown. It is also important to understand that heat input location A is merely one example. There can be multiple heat input locations, and they can be areas of larger or smaller sizes.
It is to be understood that the form of this invention as shown is merely a preferred embodiment. Various changes may be made in the function and arrangement of parts; equivalent means may be substituted for those illustrated and described; and certain features may be used independently from others without departing from the spirit and scope of the invention as defined in the following claims.
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Number | Date | Country |
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2008008512 | Jan 2008 | JP |
Entry |
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Riehl (Loop heat pipe performance enhancement using primary wick with circumferential grooves) ; Roger R. Riehl*, Nadjara dos Santos; Received Aug. 22, 2006; accepted Nov. 12, 2007. |
JP2008008512A machine translation. |