Thermal management systems

• US 8,066,055 B2
• Filed: 04/17/2009
• Issued: 11/29/2011
• Est. Priority Date: 06/30/2000
• Status: Expired due to Term

• Current Assignee: Northrop Grumman Systems Corporation (Northrop Grumman Corporation)
• Original Assignee: Alliant Techsystems Incorporated (Northrop Grumman Corporation)
• Inventors: Bugby, David C., Wolf, David A. Sr., Yun, James S., Kroliczek, Edward J.
• Primary Examiner(s): CIRIC, LJILJANA V
• Application Number:
  US12/426,001
• Publication Number:
  US 20090200006A1
• Time in Patent Office: 956 Days
• Field of Search: 165/11.1, 165/272, 165/273, 165/274, 165/104.21, 165/104.26, 165/104.33, 62/59
• US Class Current: 165/11.1
• CPC Class Codes: F25B 23/006 boiling cooling systems
• CPC Class Codes: F28D 15/0275 Arrangements for coupling heat-pipes together or with other structures, e.g. with base blocks; Heat pipe cores
• CPC Class Codes: F28D 15/043 forming loops, e.g. capillary pumped loops

Abstract

A system including a primary evaporator facilitating heat transfer by evaporating liquid to obtain vapor is disclosed. The primary evaporator receives a liquid from a liquid line and outputs the vapor to a vapor line. The primary evaporator also outputs excess liquid received from the liquid line to an excess fluid line. A condensing system receives the vapor from the vapor line, and outputs the liquid and excess liquid to the liquid line. The excess liquid is obtained at least partially from a reservoir. A primary loop includes the condensing system, the primary evaporator, the liquid line, and the vapor line, and provides a heat transfer path. Similarly, a secondary loop includes the condensing system, the primary evaporator, the liquid line, the vapor line, and the excess fluid line. The secondary loop provides a venting path for removing undesired vapor within the liquid or excess liquid from the primary evaporator.

Claims

1. A system comprising:

a condensing system operable to receive vapor from a vapor line, to condense at least some of the vapor, and to output liquid to a liquid line;

a reservoir in fluid communication with the condensing system, wherein the liquid is obtained at least partially from the reservoir;

a primary loop including the condensing system, a first evaporator, the liquid line, and the vapor line, the primary loop being operable to provide a heat transfer path;

a secondary loop including the condensing system, the first evaporator, the liquid line, the vapor line, and an excess fluid line, the secondary loop being operable to provide a venting path for removing other vapor that is present within the liquid from the first evaporator;

wherein, the first evaporator is operable to facilitate heat transfer by evaporating a received liquid to obtain a vapor, the first evaporator including a first port for receiving the liquid from a liquid line, a second port for outputting the vapor to a vapor line, a third port for outputting excess liquid received from the liquid line to an excess fluid line, and a fourth port for outputting the other vapor to a vapor line, such that the vapor line is included within the secondary loop; and

a second evaporator connected in parallel with the first evaporator, the second evaporator operable to facilitate heat transfer by evaporating a received liquid to obtain a vapor, the second evaporator including a first port for receiving the liquid from a liquid line, a second port for outputting the vapor to a vapor line, a third port for outputting excess liquid received from the liquid line to an excess fluid line, and a fourth port for outputting the other vapor to a vapor line, such that the vapor line is included within the secondary loop.

2. The system of claim 1, wherein the liquid in the first evaporator and the second evaporator received from the liquid line includes the excess liquid in excess of a liquid amount necessary to maintain saturation of a primary wick within a core of the first evaporator.

3. The system of claim 2, wherein the first evaporator and the second evaporator each includes a secondary wick that is operable to perform phase separation of the other vapor from the liquid for output through the excess fluid line.

4. The system of claim 3, wherein the primary wick and the secondary wick of the first evaporator and the second evaporator maintain capillary pumping of the liquid, the excess liquid, and the vapor, so as to maintain flow control to and through the first evaporator and the second evaporator.

5. The system of claim 1, further comprising a mechanical pump that is operable to facilitate the heat transfer by actively pumping the liquid for evaporation by the first evaporator and the second evaporator, and for output as the excess liquid through the third port to the excess fluid line.

6. The system of claim 5, wherein the reservoir is positioned between an output of the condensing system and an input of the mechanical pump.

7. The system of claim 5, wherein the mechanical pump is positioned between an input of the condensing system and an output of the first evaporator.

8. The system of claim 5, further comprising a bypass valve in parallel with the mechanical pump and operable to bypass the mechanical pump during a passive pumping operation of liquid for evaporation by the first evaporator and the second evaporator.

9. The system of claim 5, wherein the mechanical pump includes a liquid pump that is oriented in series with the liquid line and positioned between the condensing system and the first evaporator and the second evaporator.

10. The system of claim 5, wherein the mechanical pump includes a vapor compressor that is oriented in series with the vapor line and positioned between the first evaporator and the second evaporator and the condensing system.

11. The system of claim 5, further comprising:

a sensor that is operable to communicate a saturation level of a wick of the first evaporator and a wick of the second evaporator to the mechanical pump;

wherein a pumping pressure delivered by the mechanical pump is adjusted, based on the saturation level, so as to maintain saturation of the wick of the first evaporator and the wick of the second evaporator with the liquid.

12. The system of claim 5, further comprising a liquid bypass valve connected between the liquid line and the vapor line and operable to maintain constant pump speed operations of the mechanical pump.

13. The system of claim 5, wherein the first evaporator and the second evaporator each includes a primary wick, the composition of which comprises metal, and a secondary wick, the composition of which comprises metal.

14. The system of claim 1, further comprising a priming system within the secondary loop, the priming system comprising:

a secondary evaporator coupled to the vapor line; and

a secondary reservoir in fluid communication with the secondary evaporator and coupled to the first evaporator and the second evaporator by the excess fluid line;

wherein the priming system is operable to provide the liquid to the first evaporator and the second evaporator at least partially from the secondary reservoir.

15. The system of claim 14, wherein the condensing system comprises:

a first condenser within the primary loop coupled to the liquid line and to the vapor line; and

a second condenser within the secondary loop coupled to the excess fluid line and to the secondary reservoir.

16. The system of claim 1, wherein the liquid line is coaxial to and contained within the excess fluid line.

17. The system of claim 1, further comprising a back pressure regulator that is oriented in series with the vapor line and positioned between the first evaporator and the second evaporator and the condensing system, and that is operable to substantially equalize a heat load between the first evaporator and the second evaporator.

18. The system of claim 17, wherein the back pressure regulator restricts vapor from reaching the condensing system until a vapor space of the first evaporator and of the second evaporator is substantially devoid of liquid.

19. The system of claim 1, further comprising a third evaporator that is oriented in parallel with the first evaporator and the second evaporator within the primary loop.

20. The system of claim 1, wherein the condensing system comprises a plurality of condensers connected in parallel to one another.

21. The system of claim 20, further comprising:

liquid outputs associated with each of the plurality of condensers and operable to output the liquid to the first evaporator and the second evaporator; and

condenser regulators coupled to the liquid outputs and operable to regulate liquid flow therefrom.

22. The system of claim 1, further comprising:

a thermal storage unit coupled to at least one of the first evaporator and the second evaporator.

23. The system of claim 1, further comprising:

first and second flow controllers connected to the first evaporator and the second evaporator, respectively, and operable to regulate liquid flow to the first evaporator and the second evaporator, respectively, so as to ensure a substantially equal heat load distribution between the first evaporator and the second evaporator.

24. The system of claim 1, further comprising:

a condensing heat exchanger coupled to the first evaporator and the second evaporator.

25. The system of claim 24, comprising a spray-cooled evaporator coupled to the condensing heat exchanger by way of a mechanical pump.

26. The system of claim 1, wherein the condensing system comprises a body-mounted radiator.

27. The system of claim 1, wherein the condensing system comprises a deployable or steerable radiator.

28. The system of claim 1, further comprising:

a venting system configured to remove vapor bubbles from a core of the first evaporator and the second evaporator, the venting system including;

a pumping system operable to provide excess liquid to the first evaporator and the second evaporator beyond a saturation amount of liquid needed for saturating a primary wick of the first evaporator and the second evaporator, wherein the reservoir is in fluid communication with the pumping system and provides the excess liquid;

wherein the vapor bubbles are vented from the core of the first evaporator and the second evaporator through the third port of the first evaporator and the second evaporator.

29. The system of claim 28, wherein the pumping system comprises a secondary evaporator in fluid communication with the reservoir and coupled to the vapor line.

30. The system of claim 29, wherein the reservoir is in fluid communication with the secondary wick of the first evaporator and the secondary wick of the second evaporator through a mixed fluid line coupled to the third port of the first evaporator and the third port of the second evaporator.

31. The system of claim 28, wherein the pumping system comprises a mechanical pump.

32. The system of claim 31, wherein the primary wick and the secondary wick of the first evaporator and the primary wick and the secondary wick of the second evaporator maintain capillary pumping of the liquid, the excess liquid, and the vapor, so as to maintain flow control to and through the first evaporator and the second evaporator.

33. The system of claim 28, wherein the excess liquid is substantially removed from the core of the first evaporator and the core of the second evaporator through a fourth port of the first evaporator and the fourth port of the second evaporator.

34. The system of claim 1, wherein the fourth port of the first evaporator comprises a subport of the third port and wherein the fourth port of the first evaporator comprises a subport of the third port.

35. The system of claim 1, wherein

the first evaporator includes a core, a primary wick, and a secondary wick,

the second evaporator includes a core, a primary wick, a secondary wick, and wherein the first port of the second evaporator is connected in parallel with the first port of the first evaporator, the second port of the second evaporator is connected in parallel with the first port of the first evaporator, the third port of the second evaporator is connected in parallel with the first port of the first evaporator, and the fourth port of the second evaporator is connected in parallel with the first port of the first evaporator.

36. The system of claim 35, wherein the pumping system comprises a mechanical pump.

37. The system of claim 35, wherein the primary wick and the secondary wick of the first evaporator and the primary wick and the secondary wick of the second evaporator maintain capillary pumping of a liquid, the excess liquid, and a vapor, so as to maintain flow control to and through the first evaporator and the second evaporator.

38. The system of claim 35, wherein the pumping system comprises a secondary evaporator in fluid communication with the reservoir and coupled to the vapor line.

39. The system of claim 38, wherein the reservoir is in fluid communication with the secondary wick of the first evaporator and the secondary wick of the second evaporator through a mixed fluid line coupled to the third port of the first evaporator and the third port of the second evaporator.

40. The system of claim 35, wherein the excess liquid is substantially removed from the core of the first evaporator and the core of the second evaporator through a fourth port of the first evaporator and the fourth port of the second evaporator.