Crossflow micro heat exchanger

• US 6,415,860 B1
• Filed: 02/09/2000
• Issued: 07/09/2002
• Est. Priority Date: 02/09/2000
• Status: Expired due to Fees

• Current Assignee: Board of Supervisors of Louisiana State University Agricultural & Mechanical College (Louisiana State University System)
• Original Assignee: Board of Supervisors of Louisiana State University Agricultural & Mechanical College (Louisiana State University System)
• Inventors: Kelly, Kevin W., Despa, Mircea S., Harris, Chad R.
• Primary Examiner(s): FLANIGAN, ALLEN J
• Application Number:
  US09/501,215
• Time in Patent Office: 881 Days
• Field of Search: 165/164-167, 165/148, 165/151, 165/181
• US Class Current: 165/148
• CPC Class Codes: F28F 2260/02 having microchannels
• CPC Class Codes: F28F 7/02 Blocks traversed by passages for heat-exchange media F28D7/0008 takes precedence
• CPC Class Codes: Y10S 165/395 Monolithic core having flow passages for two different fluids, e.g. one- piece ceramic

Abstract

An extremely high efficiency, crossflow, fluid-fluid, micro heat exchanger is disclosed. To concurrently achieve the goals of high mass flow rate, low pressure drop, and high heat transfer rates, the heat exchanger comprises numerous parallel, but relatively short microchannels. The performance of these heat exchangers is superior to the performance of previously available heat exchangers. Typical channel heights are from a few hundred micrometers to about 2000 micrometers, and typical channel widths are from around 50 micrometers to a few hundred micrometers. The micro heat exchangers offer substantial advantages over conventional, larger heat exchangers in performance, weight, size, and cost. The heat exchangers are especially useful for enhancing gas-side heat exchange. Some of the many possible applications include aircraft heat exchange, air conditioning, portable cooling systems, and micro combustion chambers for fuel cells. The use of microchannels in a cross-flow micro-heat exchanger decreases the thermal diffusion lengths substantially, allowing substantially greater heat transfer per unit volume or per unit mass than has been achieved with prior heat exchangers. The cross-flow micro-heat exchanger have performance characteristics that are superior to state-of-the-art designs, as measured on a per-unit-volume or per-unit-mass basis.

Claims

1. A heat exchanger for transferring heat between a first fluid and a second fluid;

wherein said heat exchanger comprises first fluid channels through which the first fluid may flow, and second fluid channels through which the second fluid may flow, wherein said second fluid channels lie generally in a plane;

wherein said first fluid channels and said second fluid channels interleave, so that heat may be transferred between said first fluid channels and said second fluid channels;

wherein the direction of flow of said first fluid channels is generally perpendicular to the plane of said second fluid channels; and

wherein said heat exchanger has a density of said first fluid channels greater than about 50 per square centimeter.

2. A heat exchanger as recited in claim 1, wherein said first fluid channels are adapted for the flow of a gas, and wherein said second fluid channels are adapted for the flow of a liquid.

3. A heat exchanger as recited in claim 1, wherein the thickness of said heat exchanger, in the direction of flow of said first fluid channels, is less than about 2.0 mm.

4. A heat exchanger as recited in claim 1, wherein the thickness of said heat exchanger, in the direction of flow of said first fluid channels, is less than about 1.0 mm.

5. A heat exchanger as recited in claim 1, wherein the width of said second fluid channels, in a direction that is generally perpendicular to the direction of flow of said first fluid channels and is also generally perpendicular to the direction of flow of said second fluid channels,is less than about 500 μ

m.

6. A heat exchanger as recited in claim 1, wherein said heat exchanger has a density of said first fluid channels greater than about 200 per square centimeter.

7. A heat exchanger as recited in claim 1, wherein the thickness of said heat exchanger, in the direction of flow of said first fluid channels, is less than about 1.0 mm;

wherein the width of said second fluid channels, in a direction that is generally perpendicular to the direction of flow of said first fluid channels and is also generally perpendicular to the direction of flow of said second fluid channels, is less than about 500 μ

m; and

wherein said heat exchanger has a density of said first fluid channels greater than about 200 per square centimeter.

8. A heat exchanger as recited in claim 1, wherein said heat exchanger is fabricatedfrom a polymer.

9. A heat exchanger as recited in claim 1, wherein said heat exchanger is fabricatedfrom a ceramic.

10. A heat exchanger as recited in claim 1, wherein said heat exchanger is fabricatedfrom copper.

11. A heat exchanger as recited in claim 1, wherein said heat exchanger is fabricatedfrom aluminum.

12. A heat exchanger as recited in claim 1, wherein said heat exchanger is fabricated from metal.

13. A heat exchanger as recited in claim 1, wherein the thickness of said heat exchanger, in the direction of flow of said first fluid channels, is less than about 6.0 mm.

14. A heat exchanger as recited in claim 1, wherein the width of said second fluid channels, in a direction that is generally perpendicular to the direction of flow of said first fluid channels and is also generally perpendicular to the direction of flow of said second fluid channels, is less than about 2.0 mm.

15. A heat exchanger as recited in claim 1, wherein the thickness of said heat exchanger, in the direction of flow of said first fluid channels, is less than about 6.0 mm, and wherein the width of said second fluid channels, in a direction that is generally perpendicular to the direction of flow of said first fluid channels and is also generally perpendicular to the direction of flow of said second fluid channels, is less than about 2.0 mm.