Wound layered tube heat exchanger

• US 10,495,383 B2
• Filed: 03/01/2010
• Issued: 12/03/2019
• Est. Priority Date: 11/19/2004
• Status: Active Grant

• Current Assignee: Modine Grenada LLC (Modine Manufacturing Company)
• Original Assignee: Modine Grenada LLC (Modine Manufacturing Company)
• Inventors: Naukkarinen, Olli Pekka
• Primary Examiner(s): Leo, Leonard R
• Application Number:
  US12/715,072
• Publication Number:
  US 20110209857A1
• Time in Patent Office: 3,564 Days
• Field of Search: 165150, 165151, 165163
• CPC Class Codes: F28D 7/02 the conduits being helically coiled F28D7/10 takes precedence F28D7/0016 and F28D7/0033 take precedence
• CPC Class Codes: F28F 2240/00 Spacing means
• CPC Class Codes: F28F 9/0132 formed by slats, tie-rods, articulated or expandable rods
• CPC Class Codes: Y10T 29/49391 Tube making or reforming

Abstract

A wound tube heat exchanger 10 article that receives a heat exchange fluid and its method of manufacture. The exchanger 10 has one or more layers 12 of a tube 14. In one embodiment, the tube surface is bare. In other embodiments, the outside tube surface is enhanced to produce turbulence. At least some of the layers 12 have an ovate oblong configuration. A pair of opposing linear runs 16,18 is connected by a pair of opposing curved sections 20,22. In some embodiments, the layers are circular, oval or rectangular with radiused corners. An elongate spacer member 24 has forwardly 26 and rearwardly 28 facing edges. Defined within those edges are engagement surfaces 30 that detachably retain the opposing linear runs 16,18.

Claims

1. A heat exchanger that transfers thermal energy between an internal heat exchange fluid that flows within the exchanger and an external heat exchange fluid in thermal communication with the internal heat exchange fluid, the heat exchanger comprising:

one or more layers of a tube within which the internal heat exchange fluid passes;

at least some of the one or more layers having an oblong ovate configuration with opposing linear runs connected by opposing curved sections, the internal heat exchange fluid passing sequentially through successive ones of the linear runs;

a planar spacer member that extends perpendicularly in relation to the linear runs, the spacer member having forwardly and rearwardly facing edges, the forwardly and rearwardly facing edges each have detents spaced apart at a center-to-center distance, each detent has a major diameter and the detents are truncated and terminate at the forwardly and rearwardly facing edges at positions that are offset from the major diameters of the detents, and

wherein the opposing linear runs are detachably retained by the detents in the forwardly and rearwardly facing edges of the planar spacer member with a snap fit such that each successive ones of the linear runs are spaced apart, in an extension direction of the planar spacer member, by a distance greater than the center-to-center distance of the detents.

2. The tube heat exchanger of claim 1, wherein the forwardly facing edges and the rearwardly facing edges detachably retain successive ones of the linear runs in an alternating sequence.

3. The tube heat exchanger of claim 1, wherein each of the detents has an open portion that is less than the major diameter of the detent in order to allow the opposing linear runs to be snap fitted to the planar spacer member.

4. The heat exchanger of claim 1, wherein the tube is circular and has an outside diameter (OD), an inside diameter (ID) and a wall thickness (T=(OD-ID)/2), wherein the ratio of (T) to (OD) is between 0.01 and 0.1.

5. The heat exchanger of claim 1 wherein the spacer member assumes a hoop-like configuration.

6. The heat exchanger of claim 1 wherein the opposed curved sections are arranged in pairs and wherein the sections in a given pair have differing radii of curvature.

7. The heat exchanger of claim 1 wherein the ratio of the average radius of opposing curved sections to the tube outside diameter (OD) is approximately 10 to 3.

8. The heat exchanger of claim 1 wherein the one or more layers of a tube have one inlet and one outlet.

9. The heat exchanger of claim 1 wherein the one or more layers of a tube have multiple inlets and outlets.

10. The heat exchanger of claim 1, wherein the tube has an average outside diameter (OD), an average inside diameter (ID), and an average wall thickness (T=(OD-ID)/2), wherein the ratio of (T) to (OD) is between 0.01 and 0.1.

11. The heat exchanger of claim 1 wherein the one or more layers are provided with a surface enhancement that extends from an outside surface of the tube.

12. The heat exchanger of claim 1 wherein the one or more layers are provided with an internal surface enhancement that extends from an inside surface of the tube.

13. The heat exchanger of claim 12 wherein the internal surface enhancement is selected from the group consisting of a helical groove, a herringbone pattern, a cross-hatched pattern, a V-configuration and a tube-spiral surface texture.

14. The heat exchanger of claim 1 wherein the direction of flow within one layer of a tube is opposite from the direction of flow in the tube of another layer, such that there is cross flow between the layers.

15. The heat exchanger of claim 1 wherein the tube has a cross sectional profile selected from the group consisting of a circle, an oval, a rectangle with rounded corners, multiport, multi-channel, and combinations thereof.

16. The heat exchanger of claim 1, further including a manifold that accommodates a heat exchanger fluid that is delivered to the one or more layers of tube.

17. The heat exchanger according to claim 1 wherein the opposing linear runs includes tubes that are round and each of the detents has a frusto-circular shape.

18. The heat exchanger according to claim 1 wherein the planar spacer member is deformable in order that the opposing linear runs are capable of being snap fitted into the detents.

19. The heat exchanger according to claim 1, wherein said distance, in the extension direction of the planar spacer member, between successive ones of the linear runs is more than two times the center-to-center distance.

20. The heat exchanger according to claim 19, wherein the distance, in the extension direction of the planar spacer member, between successive ones of the linear runs is more than three times the center-to-center distance.

21. The heat exchanger according to claim 1, wherein the tube is circular and has an outside diameter, wherein the center-to-center distance of the detents is twice the outside diameter.

22. A heat exchanger that transfers thermal energy between an internal heat exchange fluid that flows within the exchanger and an external heat exchange fluid in thermal communication with the internal heat exchange fluid, the heat exchanger comprising:

one or more layers of a tube within which the internal heat exchange fluid passes, each layer including opposing linear runs connected by opposing curved sections, the internal heat exchange fluid passing sequentially through successive ones of the linear runs;

at least some of the one or more layers having a uniform bend radius; and

a planar spacer member that extends perpendicularly in relation to the one or more layers, the spacer member having forwardly and rearwardly facing edges, the forwardly and rearwardly facing edges each have engagement surfaces defining a center location in which a respective portion of the tube is received, wherein adjacent center locations are spaced apart a first distance and each of the one or more layers is detachably retained by the planar spacer member with a snap fit to the engagement surfaces of the forwardly and rearwardly facing edges, such that each successive ones of the linear runs are spaced apart, in an extension direction of the planar spacer member, by a second distance greater than the first distance between the adjacent center locations.