Modular Evaporator Assembly for a Loop Heat Pipe Thermal Control System

Information

  • Patent Application
  • 20250164194
  • Publication Number
    20250164194
  • Date Filed
    February 18, 2023
    2 years ago
  • Date Published
    May 22, 2025
    2 months ago
  • Inventors
    • Mishkinis; Donatas
    • Gottero; Marco
  • Original Assignees
Abstract
An evaporator assembly including at least one compensation chamber and at least one capillary pump that includes a primary wick, the evaporator assembly including a secondary wick extending through the at least one compensation chamber and the at least one capillary pump and contacting the primary wick thereof. The at least one compensation chamber and the at least one capillary pump are arranged parallel to one another along respective distinct axes.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS

This patent application claims priority from Italian Patent Application No. 102022000003092 filed on Feb. 18, 2022, the entire disclosure of which is incorporated herein by reference.


TECHNICAL FIELD OF THE INVENTION

The present invention relates to thermal control systems, and particularly to the thermal control of aerospace systems. In the present description reference will be made to this preferred, although not exclusive, field of application.


Specifically, the present invention relates to a modular evaporator for a Loop Heat Pipe (LHP) system.


BACKGROUND ART

LHP systems are highly efficient passive heat transfer devices based on liquid/vapor phase change in a closed and hermetically sealed loop. Fluid circulation inside the loop is produced by capillary effect. LHP systems are used as cooling devices in the thermal control of space systems.


A LHP system 100 is schematically shown in FIG. 1, and typically comprises an evaporator assembly 102 and a condenser 103. An outlet port 104 of the evaporator assembly 102 is connected to an inlet port 105 of the condenser 103 by a vapor line 106; an outlet port 107 of the condenser 103 is connected to an inlet port 108 of the evaporator assembly 102 by a liquid line 109.


The evaporator assembly 102 (FIG. 2) includes a compensation chamber 110 and a capillary pump 111 connected in series.


The capillary pump 111 is usually provided with a saddle 112 for attachment to a heat source (not shown) from which a heat flow 113 is extracted by conduction.


The capillary pump 111 includes a first micro-porous medium or primary wick 115 that surrounds, and sucks liquid from, a second porous medium or secondary wick 116 that extends throughout the compensation chamber 110 and the capillary pump 111. Secondary wick 116 is hollow and houses an inner tubing 114.


The inlet port 108 of the evaporator assembly 102 is connected to the liquid line 109 and communicates with the inner tubing 114 of the secondary wick 116.


The capillary pump 111 includes a plurality of circumferential (not shown in the Figures) and axial vapor channels 117 located on a perimeter surface of the primary wick 115 constituting a vapor-liquid interface where evaporative heat transfer takes place. Vapor flows from channels 117 to the outlet port 104, and hence to the condenser 3 through vapor line 106.


Vapor is condensed in the condenser 103, thus releasing the heat absorbed in the evaporator assembly 102. The primary wick 115 forces the liquid to return back from the condenser 103 to the evaporator assembly 102 via the liquid line 109 by capillary action. The returned liquid passes though the inner tubing 114 located inside the compensation chamber 110, cooling down the liquid in the compensation chamber 110. The compensation chamber 110 is used as a volume buffer compensator for accumulation of liquid excess during LHP operation due to temperature variations and for ensuring LHP start-up from non-operational conditions.


LHP system are simple and reliable, but suffer limitations that limit their use.


One of such limitations is the limited pumping capability of the secondary wick 116, which is not as powerful as the primary wick 115 and can pump the fluid against gravity only if the elevation difference is not more than 5-50 cm, depending on the surface tension properties of the working fluid.


Another important drawback of the limited pumping capability of the secondary wick 116 is the impossibility to create an evaporator design with multiple capillary pumps, which can cover large area for heat collecting, e. g. because the distance from the compensation chamber to the furthest capillary pump can be a restrictive factor for the LHP system performance. In this case, in fact, the elongated secondary wick can be unable to provide the necessary flow rate of liquid from the compensation chamber to the furthest capillary pump, which would lead to the primary wick dryout and, consequently, to failure in LHP operation.


Thus, the limited pumping capability of the secondary wick in the known designs of capillary pump-compensation chamber assemblies poses restrictions on the orientation of the evaporator assembly in a gravitational field and does not allow to construct long multiple evaporator assemblies.


This is clearly shown in FIG. 2, where the evaporator assembly is shown in an anti-gravity position with the capillary pump over the compensation chamber. The more is the distance between liquid level in the compensation chamber 110 and the primary wick 115 (indicated as h1), the less is the pumping capability of the secondary wick 116. When such a distance reaches a threshold level, the LHP system will stop working.


Another issue is that heat is extracted only by conduction through the small footprint of the evaporator saddle 12, which makes this solution unfit for extracting heath from large areas and/or a gas flow.


EP 3376348 A1, on the disclosure of which is based the preamble of claim 1, discloses modular evaporator units in which a plurality of evaporator assemblies of the type described above are series-connected and combined in different linear configurations.


An object of the present invention is to provide an improved modular evaporator assembly which overcomes the problems of the prior art LHPs specified above, and specifically allows to significantly extend the limits of LHP operation in any orientation in a gravity field.


A further object of the present invention is to create evaporator units configured to cover large areas and to grab heat from a gas flow.


SUMMARY OF THE INVENTION

The above object is attained by an evaporator assembly including at least one compensation chamber and at least one capillary pump including a primary wick, the evaporator assembly including a secondary wick extending through the compensation chamber and the capillary pump and contacting the primary wick, wherein the least one compensation chamber and the at least one capillary pump are arranged parallel to one another along respective distinct axes.


The parallel arrangement of compensation chamber(s) and capillary pump(s) removes the orientation constraints in a gravity field.


Preferably, the evaporator assembly includes a plurality of compensation chambers and a plurality of capillary pumps extending along respective axes that are distinct and parallel to one another.


By combining a plurality of compensation chambers and capillary pumps in different arrangements, it is possible to obtain an evaporator assembly in the form of a large “cold plate” that can be used to extract heat from an extended area and/or multiple sources.


According to an embodiment, the evaporator assembly includes a plurality of parallel branches, each branch including at least two compensation chambers or capillary pumps.


This further enhances the ability of the assembly to cover extended areas.


According to further embodiments of the invention, the evaporator assembly includes a first manifold connected to a liquid inlet port and to first ends of the compensation chambers, and a second manifold connecting respective second ends of the compensation chambers and first ends of the capillary pumps.


This arrangement simplifies connection and allows easy integration of compensation chambers and capillary pumps into a “cold plate” arrangement.


Optionally, where the system includes a plurality of branches each having two or more compensation chambers or capillary pumps, a third manifold connecting intermediate nodes of the branches can be used. This enhances a balanced liquid feed and improves the performance in transients.


According to a preferred embodiments, the compensation chambers are disposed at the opposite ends of the evaporator, and capillary pumps are arranged between the compensation chambers. Grouping the capillary pumps in a middle area of the evaporator assembly simplifies connection of the vapor outlet ports of the compensation chambers, and allows the capillary pumps to be integrated into a finned heat exchanger. This enables heat collection from a gas flow by convection.


The present invention also relates to an LHP system including at least one evaporator assembly as previously defined and at least one condenser.


A modular LHP system according to the present invention can be provided as a system that can be finally assembled and filled as a part of the integration activities of the spacecraft, as opposed to standard LHP systems that are supplied as a single-piece filled and sealed circuit, the integration of which is tricky on satellites and substantially impossible across a pressurized shell.





BRIEF DESCRIPTION OF THE DRAWINGS

For a better understanding of the present invention, a plurality of preferred embodiments are described herein by way of non-limiting examples and with reference to the accompanying drawings, wherein:



FIG. 1 is a schematic perspective view of an LHP system including a prior art evaporator assembly;



FIG. 2 is a longitudinal cross-section of the prior art evaporator assembly of the LHP system of FIG. 1;



FIG. 3 is a cross section taken along line III-III of FIG. 2:



FIG. 4 is a schematic perspective view of an LHP system including an evaporator assembly according to the present invention;



FIG. 5 is a cross section of the evaporator assembly of the heat loop of FIG. 4;



FIG. 6 is a cross section taken along line VI-VI of FIG. 5;



FIGS. 7, 8, 9 and 10 depict schematically further embodiments of the present invention;



FIG. 11 is a perspective view of an evaporator assembly according to yet another embodiment of the present invention; and



FIG. 12 is a partial cross section of the evaporator assembly of FIG. 11.





BEST MODE FOR CARRYING OUT THE INVENTION

A LHP system 1 according to the present invention, in its simplest form, is schematically shown in FIGS. 4 to 6.


As known in the art, system 1 comprises an evaporator assembly 2 and a condenser 3. An outlet port 4 of the evaporator assembly 2 is connected to an inlet port 5 of condenser 3 by a vapor line 6; an outlet port 7 of condenser 3 is connected to an inlet port 8 of evaporator assembly 2 by a liquid line 9. Evaporator assembly 2 (FIG. 5) includes a compensation chamber 10 and a capillary pump 11.


According to the present invention, and as clearly shown in FIG. 5, compensation chamber 10 and capillary pump 11 of evaporator assembly 2 are arranged parallel to one another along respective distinct axes A, B. The expression “arranged parallel to one another” as used herein refers to the spatial relationship between compensation chamber 10 and capillary pump 11, rather than their fluidic connection.


In the specific embodiment of FIG. 5, compensation chamber 10 and capillary pump 11 are also parallel-connected hydraulically, as a pair of manifolds 18, 19 connect the axial ends of compensation chamber 10 with respective ends of capillary pump 11.


Capillary pump 11 includes a first micro-porous medium or primary wick 15 that surrounds, directly contacts, and sucks liquid from, a second porous medium or secondary wick 16 extending throughout the evaporator 2, including compensation chamber 10 and manifolds 18, 19. Primary wick 15 has a typical pore size of 1-10 μm.


For example, primary wick 15 may be made of sintered metal ceramic, preferably from the mixture of stainless steel powder and fiber.


Secondary wick 16 is flexible and more permeable than primary wick 15, and has a typical pore size around 20-60 μm. Secondary wick 16 serves the purpose of supplying the primary wick 15 with liquid in case of transients due to rapid changes in power or condenser temperature.


For example, secondary wick can be made of stainless steel mesh or braided stainless steel fiber. Inlet port 8 is located at a midpoint of compensation chamber 10 and is connected to liquid feed inner tubing 14 extending through secondary wick 16 from inlet port 8 to capillary pump 11.


Specifically, liquid feed inner tubing 14 (also known as “bayonet tubing”) extends within secondary wick 16 through compensation chamber 10 from inlet port 8 to opposite ends thereof, pass through manifolds 18, 19 and enters opposite ends of capillary pump 11 through secondary wick 16. Therefore, capillary pump 11 communicates with inlet port directly through liquid feed inner tubing 14 and with compensation chamber 10 only indirectly through secondary wick 16.


Capillary pump 11 includes a plurality of circumferential (not shown in the Figures) and axial vapor channels 17 located on a perimeter surface of primary wick 15 constituting a vapor-liquid interface where evaporative heat transfer takes place. Vapor flows from channels 17 to outlet port 4, and hence to condenser 3 through vapor line 6.


Vapor is condensed in the condenser 3, thus releasing the heat absorbed in the evaporator assembly 2. Primary wick 15 forces the liquid to return back from the condenser 3 to the evaporator assembly 2 via the liquid line 9 by capillary action. The returned liquid passes though inner tubing 14 located inside the compensation chamber 10, cooling down the liquid in the compensation chamber 10. The compensation chamber 10 is used as a volume buffer compensator for accumulation of liquid excess during LHP operation due to temperature variations and for ensuring LHP start-up from non-operational conditions.


For proper operation, the compensation chamber 10 always has two phases inside, liquid and vapor, which are separated by a vapor-liquid interface. The compensation chamber 10 plays a critical role during transients such as rapid input power drop down or rise up and/or quick variations of the condenser temperature.


As shown in FIG. 5, where the evaporator assembly is shown in an antigravity position with capillary pump 11 above compensation chamber 10, the distance between the liquid level in compensation chamber 10 and primary wick 15 is h2, which can be kept much smaller than h1 in FIG. 2 if compensation chambers of the same volume are used. This shows that the pumping capability of secondary wick 16 is no longer a critical factor.


Evaporator assembly 2 of FIG. 5 can be seen as an elementary module, starting from which larger and more complex evaporator assemblies can be developed, as shown in FIGS. 7-10. The same numerals are used to reference parts that are similar or corresponding to parts of the embodiment of FIG. 5.


In the embodiment of FIG. 7, evaporator assembly 2 is composed of two compensation chambers 10 connected hydraulically in parallel by manifolds 18, 19. Evaporator assembly 2 also includes a capillary pump 11 arranged parallel to and in between the two compensation chambers 10. Manifold 18 is connected to liquid line 9 at respective first ends of compensation chambers 10, manifold 19 is connected to second ends of the compensation chambers 10 and to capillary pump 11. Vapor outlet 4 at an opposite end of capillary pump 11 is connected to vapor line 6.


The secondary wick 16 extending along compensation chambers 10, capillary pump 111 and manifolds 18, 19 is shown schematically by dotted lines.



FIGS. 8, 10 show different, more complex embodiments of the invention. Primary and secondary wicks 15, 16 not shown, and only steady-state flow is indicated schematically.


The embodiment of FIG. 8 is very similar to that of FIG. 7, but includes two capillary pumps 11 arranged parallel to one another and in between the two compensation chambers 10. Manifold 18 connects liquid line 9 to first ends of compensation chambers 10, manifold 19 connects second ends of compensation chambers 10 with first ends of capillary pumps 11. Vapor outlet ports 4 at second ends of capillary pumps 11 are connected to vapor line 6.


The embodiment of FIG. 9 is very similar to that of FIG. 8, and further includes a third compensation chamber 10 disposed in between the two capillary pumps 11. As described for the embodiment of FIG. 8, manifold 18 connects liquid line 9 to first ends of compensation chambers 10, manifold 19 connects second ends of compensation chambers 10 with first ends of capillary pumps 11. Vapor outlet ports 4 at second ends of capillary pump 11 are connected to vapor line 6.



FIG. 10 discloses an embodiment with a plurality of compensation branches 20 and three capillary pump branches 21 arranged parallel to one another Rather than having a single compensation chamber 10 or a single capillary pump 11 for each branch, the LHP system 1 of FIG. 10 includes two compensation chambers 10 in each compensation branch 20 and two capillary pumps 11 in each capillary pump branch 21.


It is clear that this modular approach can be further extended by combining a number of elementary modules to form an evaporator assembly 2 of any dimensions.



FIG. 11 discloses an example of a physical embodiment of an evaporator assembly 2 according to the present invention.


Evaporator assembly 2 of FIG. 11 includes four compensation branches 20 each including two compensation chambers 10, and five pump branches each including two capillary pumps 11. All of the branches 20, 21 are arranged parallel to one another. Compensation branches 20 are located at the sides of the assembly, two on each side; pump branches 21 are in the middle.


Manifolds 18, 19 connect respective first ends and second ends of the branches 20, 21. An additional manifold 24 connects intermediate nodes of the branches 20, 21, in between each pair of compensation chambers 10 and capillary pumps 11. Manifold 18 is connectable to liquid line 9. Vapor outlet ports 4 of each of the capillary pumps 11 are connected to a vapor manifold 25, which is in turn connectable to vapor line 6).


The parallel arrangement of the capillary pump branches 21 allows the latter to be incorporated as a tube bundle in a finned heat exchanger 22 having a pack of parallel fins 26, of which only a few are schematically depicted in FIG. 1. Capillary pump branches 21 run across fins 26, in conductive contact therewith. FIG. 12 shows heat exchanger 22 in cross section and a gas flow 25 from which heat exchanger 22 may extract heat.


Finally, it is evident that further configurations and modifications of the evaporator assembly 2 and the resulting LHP system are possible without departing from the scope of the present invention as defined by the claims.

Claims
  • 1. An evaporator assembly (2) comprising: at least one compensation chamber (10) and at least one capillary pump (11) comprising a primary wick (15), the evaporator assembly (2) including a secondary wick (16) extending through the at least one compensation chamber (10) and the at least one capillary pump (11) and contacting the primary wick (15) thereof, characterized in that the at least one compensation chamber (10) and the at least one capillary pump (11) are arranged parallel to one another along respective distinct axes (A, B).
  • 2. The evaporator assembly as claimed in claim 1, including a plurality of compensation chambers (10) and a plurality of capillary pumps (11) arranged parallel to one another.
  • 3. The evaporator assembly as claimed in claim 2, including a plurality of parallel branches (20, 21), each branch including at least two compensation chambers (10) or capillary pumps (11).
  • 4. The evaporator assembly as claimed in claim 3, including a first manifold (18) connected to a liquid inlet port (8) and to first ends of the compensation chambers (10) and a second manifold (19) connecting respective second ends of the compensation chambers (10) and first ends of the capillary pumps (11).
  • 5. The evaporator assembly as claimed in claim 3, wherein the compensation chambers (10) are disposed at opposite sides of the evaporator assembly (2), the capillary pumps (11) being arranged between the compensation chambers (10).
  • 6. The evaporator assembly as claimed in claim 3, characterized in that the capillary pumps (11) form a tube bundle of a finned heat exchanger configured to extract heat from a gas flow.
  • 7. The evaporator assembly as claimed in claim 3, characterized in that the capillary pumps (11) form a tube bundle connected by common thermally conductive plates configured to extract heat from an extended surface area.
  • 8. The evaporator assembly as claimed in claim 3, wherein vapor outlet ports (4) of the capillary pumps (11) are connected to a common vapor outlet manifold (25).
  • 9. A loop heat pipe (LHP) system including at least one evaporator assembly (2) as claimed in claim 1 and at least one condenser (3).
Priority Claims (1)
Number Date Country Kind
22425006.8 Feb 2022 IT national
PCT Information
Filing Document Filing Date Country Kind
PCT/IB2023/051492 2/18/2023 WO