1. Field of the Invention
This invention relates generally to semiconductor device systems, and more particularly to methods and apparatus for thermally managing semiconductor chips and related devices.
2. Description of the Related Art
Many types of modern integrated circuits, implemented in semiconductor chips for example, dissipate significant amounts of power in the form of heat. If not managed properly, the generated heat may quickly build up and reduce the performance or even cause the failure of such circuits. The task of removing heat build up from a modern semiconductor chip is complicated by several factors. The first factor is the non-uniform structure of current chips. The structure of a typical semiconductor chip varies greatly from edge to edge and from top to bottom. Some areas have higher circuit density or more metallization than others. This leads to areas of relatively higher heat flux or “hot spots”. The second factor complicating heat management is the tendency for hot spots to move around. Such movements are usually the result of different parts of the chip drawing more power than others at different times depending on the tasks being performed.
A basic conventional form of heat management system for some semiconductor chips is a heat sink, usually with multiple fins, that is placed in contact with the chip. With a relatively large surface area, such sinks rely on conduction, convection and to a lesser extent radiative heat transfer to remove heat from the chip.
A more complicated conventional heat transfer system for some devices includes a micro-channel heat exchanger that is placed in thermal contact with the device. In one conventional design, the micro-channel has a small internal chamber filled with tiny plates that enhance the overall internal surface area. A coolant, typically water, is inside the chamber and circulated by capillary and thermal expansion action or by way of a pumping device. In some designs, the portions of the coolant alternatively vaporize and then condense to liberate heat.
In one particular form of microchannel that utilizes such two-phase flow, a gas permeable membrane is placed inside the micro-channel to divide the interior into a fluid chamber and a vapor chamber. The conventional membrane is fully porous across its entire length (i.e., substantially consistent properties across its length). Vapor formed in the liquid side of the microchannel passes through the membrane and into the vapor chamber where it is vented to atmosphere. The venting of bubbles into the membrane is necessary. Otherwise, bubbles would be held stationary by capillary forces and block liquid from rewetting active surfaces, or consume a large fraction of the flow cross section and add significant flow resistance inside the liquid chamber. Such flow disturbances can cause oscillations or even excursive flow instabilities.
Mechanical strength is one issue associated with the fully porous vapor membrane. Thermal cycling of micro-channel heat exchangers can cause significant mechanical stresses. Thermal conductivity is another issue, since the porous material is not as thermally conductive as, say, a material with a higher density.
An embodiment of the present invention is directed to overcoming or reducing the effects of one or more of the foregoing disadvantages.
In accordance with one aspect of an embodiment of the present invention, a method of thermally managing a heat generating device is provided that includes placing a heat exchanger in thermal communication with the heat generating device. The heat exchanger has an interior space. A membrane is in the interior space between a first chamber and a second chamber. The membrane has a gas impermeable portion and at least one gas permeable portion to enable vapor bubbles in the second chamber to pass through the membrane at the at least one gas permeable portion and into the first chamber. A liquid is moved through the second chamber.
In accordance with another aspect of an embodiment of the present invention, a method of thermally managing a heat generating device is provided that includes placing a heat exchanger in thermal communication with the heat generating device. The heat exchanger has an interior space. A membrane is in the interior space between a first chamber and a second chamber. The membrane has at least one gas permeable portion. A mechanism is provided to selectively enable and disable fluid communication between the at least one gas permeable portion and the second chamber. A liquid is moved through the second chamber.
In accordance with another aspect of an embodiment of the present invention, an apparatus is provided that includes a heat exchanger that has an interior space. A membrane is in the interior space and between a first chamber and a second chamber. The membrane has a gas impermeable portion and at least one gas permeable portion to enable vapor bubbles in the second chamber to pass through the membrane at the at least one gas permeable portion and into the first chamber.
In accordance with another aspect of an embodiment of the present invention, an apparatus is provided that includes a heat exchanger that has an interior space. A membrane is in the interior space between a first chamber and a second chamber. The membrane has at least one gas permeable portion. A mechanism is provided to selectively enable and disable fluid communication between the at least one gas permeable portion and the second chamber.
The foregoing and other advantages of the invention will become apparent upon reading the following detailed description and upon reference to the drawings in which:
Various embodiments of a heat exchanger for use with an electronic device are described herein. One example includes a membrane with gas permeable portions and relatively impermeable portions. Another example includes moveable gates to selectively allow vapor to cross a membrane. Additional details will now be described.
In the drawings described below, reference numerals are generally repeated where identical elements appear in more than one figure. Turning now to the drawings, and in particular to
In this illustrative embodiment, the heat exchanger 10 includes a base substrate 35, a vapor transfer membrane 40 positioned on the base substrate 35, an upper substrate 45 positioned on the vapor membrane 40 and a cover 50 positioned on the upper substrate 45. A rectangular footprint is depicted. However, the heat exchanger 10 may have other shapes if desired. Fluid ports 55 and 60 are connected to the heat exchanger 10 for the delivery and removal of coolant 65. The coolant may be water, alcohol, glycol or other liquids suitable for heat transport. The ports 55 and 60 are in fluid communication with a pump 70. The pump 70 may include not only the ability to move fluid, but also the capacity to refrigerate the coolant 65 if desired. In addition, the pump 70 may include or otherwise be provided with a heat sink in order to reduce the temperature of the circulating coolant 65. A vapor vent 75 is provided in the cover 50 in order to liberate coolant vapor 80 that goes into vapor phase during movement through the heat exchanger 10.
Additional details of the heat exchanger 10 may be understood by referring now to
The base substrate 35 may be formed in the shape of a basin. The base substrate 35, the upper substrate 45 and the cover 50 provide an interior space in which the vapor membrane 40 is positioned. The base substrate 35 and the overlying vapor membrane 40 define a flow chamber 95 through which the coolant 65 passes. The coolant 65 is introduced into the port 55 and traverses a bore that is formed in the cover 50, the upper substrate 45 and the vapor membrane 40 leading to the flow chamber. The outlet port 60 is similarly in fluid communication with the corresponding outlet bore 105 that traverses the vapor membrane 40, the upper substrate 45 and the cover 50. The coolant 65 is preferably liquid phase upon introduction into the flow chamber 85, but some vapor phase may be present as well. One function of the base substrate 35 is to provide a low thermal resistance conductive heat transfer pathway from the semiconductor chip 15. Accordingly, the base substrate 35 is advantageously fabricated from thermally conductive materials, such as copper, nickel, silver, aluminum, combinations of these or the like. A thermal interface material (not shown), such as a thermal paste, grease or gel, may be positioned between the base substrate 35 and the semiconductor chip 15 to facilitate conductive heat transfer.
The upper substrate 45 is fashioned with a frame-like design such that an internal vapor chamber 110 is defined between the vapor membrane 40 and the cover 50. In this sense, the vapor membrane 40 is between the flow chamber 95 and the vapor chamber 110. Like the base substrate 35, the upper substrate 45 is advantageously fabricated from thermally conductive materials, such as copper, nickel, silver, aluminum, combinations of these or the like. Well-known adhesives, such as epoxies, may be used to secure the upper substrate 45 to the vapor membrane 40 and the cover 50. Optionally, other fastening methods may be used, such as clamps, screws or the like. The cover 50 may be composed of the same types of materials as the upper substrate 45. The vent 75 in the cover 50 may be a circular bore or other shape. Multiple vents may be used if desired.
As the coolant 65 traverses the chamber 95, bubbles 115 may form depending upon the temperature and flow rate. Unlike a conventional vapor membrane, the vapor membrane 40 is not a gas permeable film. Instead, the vapor membrane 40 includes gas permeable portions, two of which are visible in
The relatively gas impermeable remainder of the membrane 40 may be composed of a variety of materials, such as, for example, copper, silicon, aluminum, gold, nickel or the like. In one embodiment, suitable openings may be formed in the membrane 40 to accommodate the gas permeable portions 120 and 125, which may be secured therein by the act of deposition itself, adhesives or other fastening techniques. In another embodiment, the membrane 40 may be fabricated from a gas permeable material of the types just described and thereafter coated with an impermeable material in a pattern that yields the permeable portions 120 and 125.
Since the membrane 40 may be only a few tens of microns thick, mechanical strength is a design issue. However, since many areas of the membrane 40 may be formed from relatively non-porous and thus higher strength materials, the overall mechanical strength of the membrane 40 will be greater than a comparably sized fully porous membrane. The vapor membrane 40 may by secured to the base substrate 35 by way of well-known adhesives, such as epoxies.
It should be understood that the terms “gas impermeable” are not used herein as absolutes. Indeed, even such dense materials as concrete and steel are gas permeable to a small extent. Thus, it should be understood that gas impermeable as used herein is intended to mean much lower gas permeability than the gas permeable portions 120 and 125.
Although two phase flow can often be problematic from a fluid transport standpoint, Applicants have discovered that certain advantages flow from the generation of the vapor bubbles 115 during the movement of the coolant 65 through the chamber 95. In particular, Applicants have ascertained that a higher heat flux from the semiconductor chip or other device being cooled may be obtained wherever the vapor bubbles 115 form. To capitalize on this effect, the heat exchanger 10, and in particular the base substrate 35, may be provided with one or more nucleation sites, two of which are visible and labeled 130 and 135 respectfully. The nucleation sites 130 and 135 are designed to more readily foster the formation of the vapor bubbles 115. The position and size of the nucleation sites 130 and 135 may be tailored to correspond to areas of higher heat flux from the semiconductor chip 15. It is a relatively straight forward matter to thermally map a semiconductor chip to ascertain those positions known as hot spots. In this way, the nucleation sites 130 and 135 may be positioned and dimensioned to correspond to those hot spots of the semiconductor chip 15 that present the highest heat flux. Areas of relatively lower heat flux from the semiconductor chip 15 are still cooled by the heat exchanger 10. The gas permeable portions 120 and 125 may be advantageously positioned proximate respective of the nucleation sites 130 and 135. In this way, for example, bubbles 115 liberated from the nucleation site 130 may quickly move into the gas permeable portion 120 and ultimately the vapor chamber 110. In this way, vapor bubbles 115 may be quickly removed from the fluid chamber 95 so that desirable heat flux is achieved while avoiding flow blockage, diminished fluid flow rate and other issues associated with two-phase flow. The portion of
Attention is now turned to
Some care should be exercised in managing the behavior of the coolant vapor 80 after it enters the vapor chamber 110. It is known that the vapor 80 that is transferred from the flow chamber 95 to the vapor chamber 110 will undergo a change in pressure and a change in temperature, causing some condensation. A few exemplary condensate droplets are shown in either side of the gas permeable portion 120 and labeled 147. The condensed vapor 147, if not evacuated from the vapor chamber 110, could clog the gas permeable portion 120 and inhibit performance. To avoid this scenario, a surface treatment 149 can be applied to the area surrounding the gas permeable portion 120 that will induce motion of the condensed vapor droplets 147 away from the gas permeable portion 120. One type of exemplary surface treatment 149 will create a wettability gradient that drives fluid away from the gas permeable portion 120. In the case of chemical phase separation, surface treatments or additional chemical structures could be applied to this same region to induce, for example, favorable chemical reactions or decontamination of the gas phase before it is evacuated from the vapor chamber. Examples include surface coatings of carbon nanotubes, or nanopillar silicon, either aligned or randomly oriented. Additionally, nanopillars of metals and semiconducting alloys including SiGe, gold, or the like could be used etc. Characteristic pore sizes range from 50 nm to 100 microns. The use of these localized and directional vapor condensate transport and/or treatment schemes would not be possible in prior devices that contain a uniformly porous membrane.
Additional detail of the base substrate 35 may be understood by referring now to
In an alternate exemplary embodiment, the interior of the base substrate may be altered to facilitate greater heat transfer. In this regard, attention is now turned to
In the foregoing illustrative embodiment, pathways through the vapor membrane are fixed in advance by pre-selecting the sites for gas permeable versus non-gas permeable portions of the vapor membrane. However, in an alternate exemplary embodiment, the gateways for vapor through the vapor membrane may be dynamically selected based upon the thermal activity of an underlying device and using a mechanism designed to enable selective access. In this regard, attention is now turned to
Additional detail of the membrane gate array may be understood by referring now to
A variety of actuators may be used to open and close the various gates 235, 240, etc. One illustrative embodiment may be understood by referring now to
Attention is now turned to
In an alternate exemplary embodiment, a different type of actuator and gate may be used to selectively open and close openings leading to the vapor membrane. In this regard, attention is now turned to
It should be understood that the heat exchanger embodiments 10 or 10′ may be used in a variety of different electronic devices, one of which is shown in schematic form in
While embodiments of the invention may be susceptible to various modifications and alternative forms, specific embodiments have been shown by way of example in the drawings and have been described in detail herein. However, it should be understood that the invention is not intended to be limited to the particular forms disclosed. Rather, the invention is to cover all modifications, equivalents and alternatives falling within the spirit and scope of the invention as defined by the following appended claims.
This application claims benefit under 35 U.S.C. 119(e) of prior provisional application Ser. No. 61/186,674, filed Jun. 12, 2009.
Number | Date | Country | |
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61186674 | Jun 2009 | US |