Plate fin heat exchanger

• US 4,434,842 A
• Filed: 11/24/1981
• Issued: 03/06/1984
• Est. Priority Date: 12/02/1980
• Status: Expired due to Fees

• Current Assignee: IMI Marston Ltd. (IMI PLC)
• Original Assignee: IMI Marston Ltd. (IMI PLC)
• Inventors: Gregory, Edward J.
• Primary Examiner(s): Richter, Sheldon J.
• Application Number:
  US06/324,568
• Time in Patent Office: 833 Days
• Field of Search: 62/527, 165/133, 165/166
• US Class Current: 165/133
• CPC Class Codes: F28F 13/187 especially adapted for evaporator surfaces or condenser surfaces, e.g. with nucleation sites
• CPC Class Codes: F28F 3/027 with openings, e.g. louvered corrugated fins; Assemblies of corrugated strips

Abstract

A heat exchanger in which liquids are boiled, the heat exchanger being provided with fins in the boiling region, the fins comprising a corrugated layer formed of two sheets, each sheet being apertured, the sheets being in close proximity one to the other such that nucleation of bubbles occurs between the sheets and the bubbles are released by the apertures in the sheets.

Claims

1. A plate fin heat exchanger for boiling a liquid, the heat exchanger having a plurality of stacked spaced plates of fluid impervious material adapted and arranged to be heated in use on the first side and to have a liquid to be vaporized on the second side, the second sides of adjacent plates facing each other, there being located between adjacent second sides at least one fin extending, in use, into the liquid to be vaporized, the fin being a separate item formed separately from the plates, wherein the improvement comprises the fin being of at least two layers at least in part having a small gap therebetween, one at least of the outer layers having a plurality of holes therein.

2. A heat exchanger as in claim 1 in which the at least one fin has two layers, and each layer has a plurality of holes therein, some at least of the holes being non-coincident between the two sheets.

3. A heat exchanger as in claim 1 in which the at least one is metal and the layers touch over part of their area.

4. A heat exchanger as in claim 1 in which, in at least part of the heat exchanger, all of the fins in the portion of the heat exchanger adapted to boil liquids are in the improved form.

5. A heat exchanger as in claim 1 in which the at least one fin is formed of aluminium and in which it is brazed to the fluid impervious surface.

6. A heat exchanger as in claim 1 in which the gap between the layers of the at least one fin is in the region 2 to 50 microns.

7. A heat exchanger as in claim 6 wherein said gap is in the region 2 to 10 microns.

8. A heat exchanger as in claim 6 wherein said gap is 5 microns.

9. A heat exchanger as in claim 6 wherein the holes have a diameter in the range 100 to 3,000 microns.

10. A heat exchanger as in claim 6 wherein the holes have a diameter in the range 500 to 2,000 microns.

11. A heat exchanger as in claim 9 wherein the holes are disposed at an overall density of 5 to 10/cm².

12. A heat exchanger as in claim 11 wherein the holes are disposed at an overall density of 6/cm².

13. A heat exchanger as in claim 1 wherein the thickness of each layer of the at least one fin is in the range 0.1 to 0.3 mm.

14. A heat exchanger as in claim 13 wherein the thickness of each layer of the at least one fin is in the range 0.1 to 0.2 mm.

15. A heat exchanger as in claim 13 wherein the thickness of each layer of the at least one fin is 0.15 mm.

16. A heat exchanger as in claim 1 in which the at least one fin is formed by superimposing two or more layers of apertured sheets one above the other and corrugating the superimposed sheets.