This invention relates in general to cooling techniques and, more particularly, to cooling techniques which facilitate control of temperatures and temperature gradients within a structure being cooled.
There are a variety of types of applications in which there is a need to control temperatures and/or temperature gradients within a structure being cooled. One example is phased array antenna systems, which are used in a number of different contexts, such as satellites and other space vehicles. A phased array antenna system includes an array of antenna elements that are separately controlled by respective circuit portions. Wavefronts transmitted and received by the antenna system are represented electrically by respective signals at the various antenna elements, and these electrical signals have phases which typically vary from antenna element to antenna element across the array. Consequently, it is important that the circuit portions associated with respective antenna elements introduce equal amounts of phase delay into the signals passing through them. Variations in the phase characteristics of the different circuit portions are undesirable, because such variations can introduce distortion into transmitted wavefronts and received wavefronts.
The circuit portions used to control the antenna elements in existing phased array antenna systems have phase characteristics that inherently vary with temperature. Consequently, in order to avoid undesirable phase variations between electrical signals in the circuit portions for different antenna elements, it is desirable that all of the circuit portions for all of the antenna elements operate at substantially the same temperature. In other words, it is desirable to avoid any significant temperature gradients across the array.
Various cooling techniques have previously been developed to attempt to avoid temperature gradients across the circuitry of phased array antenna systems. Some approaches utilize a single-phase or two-phase coolant which is mechanically pumped. However, mechanically pumping these coolants requires an external source of energy to drive the pump, and the use of a mechanical pump presents reliability concerns as a result of the possibility of a mechanical failure. The reliability considerations are of particular concern with respect to environments such as a space vehicle, where repairs can be difficult or impossible.
A different approach uses heat pipes. However, since a phased array antenna system typically has a two-dimensional array of antenna elements, heat pipes represent a one-dimensional attempt to solve a two-dimensional problem. In particular, a layer of parallel heat pipes can be provided to transport high heat fluxes in directions parallel to the heat pipes, but it is not possible to distribute heat in a transverse direction without adding a second layer of heat pipes that extends transversely to the first layer. The second layer of heat pipes increases the size and weight of the system, and is not as effective as the first layer in distributing heat, due to the conductive resistance between the two layers of heat pipes. In a phased array antenna system in which the circuitry is provided in a configuration commonly known as a slat architecture, the use of even a single layer of heat pipes may be difficult or impossible, due to dimensional limitations inherent in the system.
From the foregoing, it may be appreciated that a need has arisen for an improved method and apparatus to effect cooling of a structure where varying temperature gradients are undesirable. The present invention provides a method and apparatus to address this need.
A first form of the invention involves a technique for cooling an apparatus which includes an antenna section with a plurality of antenna elements, and circuitry having a plurality of circuit portions each operatively coupled to a respective one of the antenna elements. Capillary pressure of a cooling fluid within a wick in a loop is utilized to urge the fluid to travel around the loop, the wick being disposed within the loop in the region of the circuitry.
A second form of the invention involves: providing in the region of heat-generating structure a plurality of evaporators which each include a wick; utilizing capillary pressure of the fluid within the wicks to urge the fluid to travel around the loop; distributing fluid flowing through the loop among the evaporators with a manifold section having a plurality of first passageway sections which each have an inlet end and which each have an outlet end coupled to an input of a respective evaporator, and having a plurality of second passageway sections that each have a first end which is approximately normal to and communicates with a respective first passageway section, and that each have a second end which is coupled to the first end of a different first passageway section.
A third form of the invention involves: providing in the region of heat-generating structure a plurality of evaporators which each include a wick; utilizing capillary pressure of the fluid within the wicks to urge the fluid to travel around the loop; distributing fluid flowing through the loop among the evaporators in a sequence corresponding to a progressive increase in the respective amounts of heat accepted by the evaporators from the structure.
A better understanding of the present invention will be realized from the detailed description which follows, taken in conjunction with the accompanying drawings, in which:
Referring again to
The cooling system 14 includes a plurality of evaporators 61–70, which are each disposed between a respective pair of two adjacent slats 31–50. Each evaporator 61–70 accepts heat generated by the two adjacent slats, and transfers it to a cooling fluid which is flowing through that evaporator, causing the fluid to change from a liquid state to a vapor state, as discussed in more detail later. The resulting vapor then exits the evaporators 61–70 and enters a vapor header 76, and travels through the vapor header 76 in a direction indicated by an arrow 77.
The cooling system 14 includes a plurality of condensers 81–86, each of which has an inlet coupled to the vapor header 76. The embodiment of
The cooling system 14 includes a reservoir 93, which is in fluid communication with the liquid return line 89 at a location between the outlets of condensers 81–86 and the inlets of evaporators 61–70. The reservoir 93 could alternatively communicate with the liquid return line 89 at some other location along the length of the liquid return line 89. A temperature sensor 94 is provided on the reservoir 93, in order to sense the temperature of cooling fluid disposed within the reservoir 93. A heater 96 is controlled by the sensor 94, and can supply heat to the cooling fluid within the reservoir 93, in order to increase the temperature of the cooling fluid.
In the disclosed embodiment, the heat sink 88 is highly efficient, and the liquid exiting each condenser 81–86 is sub-cooled to a temperature lower than that needed for proper operation of the evaporators 61–70. This subcooling of the liquid coolant is indicated diagrammatically at 111 and 112 in
The sub-cooled liquid exiting the condensers 81–86 is supplied through the liquid return line 89 to a manifold 121, which facilitates an efficient distribution of the cooling fluid among the evaporators 61–70. The manifold 121 include several T-junctions, two of which are indicated by broken lines at 123 and 124 in
The manifold 121 is configured to supply fluid to evaporators 61–70 in an order based on the respective amount of heat absorbed by each evaporator under normal operating conditions. In this regard, and with reference to
The manifold 121 distributes the cooling fluid to the slats in an order corresponding to the amount of heat typically dissipated by each slat, from the slats that dissipate the least heat progressively to the slats that dissipate the most heat. Thus, the manifold 121 distributes cooling fluid first to the evaporators 61 and 70 for the outermost slats, then to nearby evaporators, and finally to the evaporators in the center of the array, such as the evaporator 66.
An isolator of a known type can optionally be provided at the inlet to each of the evaporators 61–70, as indicated diagrammatically at 141–143 in
The cooling system shown in
As the cooling fluid in the wick changes phase from a liquid to a vapor, there is a vapor pressure increase in the region of this phase change, which causes cooling fluid within the wick to move. This capillary pressure within each wick causes the cooling fluid to travel around the loop shown in
When the vapor in the vapor header 76 reaches the condensers 81–86, the condensers transfer heat from the vapor to the heat sink 88, thereby cooling the vapor sufficiently so that it condenses back into a liquid. The heat sink 88 is somewhat oversized, so as to extract more heat than necessary from the cooling fluid. As result, the cooling fluid exiting the condensers 81–86 is sub-cooled, thereby cold biasing the system. In other words, the cooling fluid leaving the condensers 81–86 and entering the liquid return line 89 has a temperature which is less than the fluid temperature that will cause the evaporators to operate with optimum efficiency.
The cooling fluid in the liquid return line 89 has, of course, a high thermal transport capacity. The heater 96 at the reservoir 93 is used to bring the sub-cooled liquid in the liquid return line 89 up to a suitable temperature for introduction into the evaporators 61–70. In this regard, the reservoir 93 contains a quantity of the cooling fluid, part of which will be in a liquid form and part of which will typically be in vapor form. The temperature sensor 93 senses the temperature of the cooling fluid within the reservoir 93, for example in a central region that typically contains a mixture of the liquid and vapor. The sensor 94 controls the heater 96 in a manner so that the heater 96 supplies heat to the liquid portion of the fluid in the reservoir 93. By maintaining the fluid in the reservoir 93 at a selected temperature which corresponds to optimal operation of the evaporators, the thermal transport capacity of the cooling fluid maintains the cooling within the liquid return line 89 at approximately this same temperature, so that the cooling fluid reaching each evaporator is at the temperature which facilitates optimal operation.
The reservoir 93 also functions to provide cooling liquid inventory for variable operating conditions. More specifically, the phased array antenna system is capable of operating in different modes, and the circuitry on the slats will generate significantly more heat in some operating modes than in other operating modes. Thus, the cooling system 14 must dissipate significantly more heat during some operating modes than during other operating modes, which in turn affects the amount of heat in the cooling fluid and thus the proportion of vapor to liquid throughout the system. The reservoir accommodates these changes in operating conditions by keeping the main cooling loop full of cooling fluid, regardless of variations in the proportion of vapor to liquid.
As fluid from the liquid return line 89 enters the manifold 121, the T-junctions (including those at 123–124) facilitate an appropriate distribution of cooling fluid among the evaporators. In this regard, if the T-junctions were omitted and the cooling fluid was supplied in a uniform and parallel manner to the inlets of all of the evaporators, evaporators absorbing greater amounts of heat would tend to deprive evaporators absorbing smaller amounts of heat of sufficient cooling fluid. Consequently, in this disclosed embodiment, the evaporators which absorb the largest amounts of heat are the last evaporators to receive fluid from the manifold 121, and help to draw fluid through the manifold 121 past the inlets of evaporators that absorb smaller amounts of heat. Further, the T-junctions (including those at 123 and 124) help to direct fluid flow straight into the inlets of the evaporators that absorb smaller amounts of heat, while allowing some of that fluid flow to be drawn off at a right angle to flow to other evaporators that absorb larger amounts of heat.
If the optional isolators are provided, such as those shown at 141–143, each isolator acts to trap any vapor bubbles that may be present in the liquid passing through it, and to hold those bubbles until they condense or collapse back into liquid form.
A portion of the circuit board 226 is broken away in
As mentioned above, the cooling system shown in
More specifically,
Cooling fluid enters the evaporator 310 through the inlet tube 317, as indicated diagrammatically by an arrow 321. This fluid then enters the wick 316. Some of the fluid exiting the tube 317 flows back along the outside of the tube 317 until it can enter the wick 316. Heat absorbed by the evaporator 310 causes the liquid within the wick 316 to change to a vapor, and to then exit the evaporator 310 through an outlet, as indicated diagrammatically by an arrow 324. Fluid flow through the evaporator 310, and thus around the loop, is effected by capillary pressure within the wick 316, in a manner similar to that discussed above in association with
The present invention provides a number of technical advantages. One such advantage is that use of a cooling system driven by capillary pressure provides sufficient cooling to minimize temperature gradients across an antenna array of a phased array antenna system, while also providing effective control of the temperatures within the array. A related advantage is that these features are achieved without the weight or expense of overlapping sets of heat pipes, or additional electronic circuitry. Another advantage is that, where the cooling system is configured as a capillary pumped loop, a liquid reservoir of the loop provides sufficient fluid inventory to accommodate variable heat generation by the array over time, as well as variable heat generation across the array.
A different advantage results from the provision of a cooling system which has a number of evaporators that effect a flow of cooling fluid through capillary pressure, and which includes a manifold that distributes cooling fluid efficiently to each evaporator. A related advantage is realized where the manifold supplies cooling fluid successively to the evaporators, in an order corresponding to a progressive increase in the amounts of heat dissipated by the evaporators. Another advantage is realized where the manifold effects fluid distribution to successive evaporators through a series of T-junctions which each permit fluid flow into a respective evaporator through a straight first passageway section, while drawing off some fluid for subsequent evaporators through a second passageway section which is generally perpendicular to the first passageway section.
Although selected embodiments have been illustrated and described in detail, it will be understood that various substutions and alterations are possible without departing from the spirit and scope of the present invention, as defined by the following claims.
This application claims the priority under 35 U.S.C. §119 of provisional application No. 60/421,373 filed Oct. 24, 2002.
Number | Name | Date | Kind |
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5816313 | Baker | Oct 1998 | A |
5829519 | Uthe | Nov 1998 | A |
6205803 | Scaringe | Mar 2001 | B1 |
20050061487 | Kroliczek et al. | Mar 2005 | A1 |
Number | Date | Country | |
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60421373 | Oct 2002 | US |