Heat exchange tubes and tube assembly configurations

Patent metadata

Field	Value
Publication number	US-10415892-B2
Application number	US-201715849416-A
Country	US
Kind code	B2
Filing date	Dec 20, 2017
Priority date	Dec 20, 2017
Publication date	Sep 17, 2019
Grant date	Sep 17, 2019

Abstract

A heat exchange tube for an HVAC system can include at least one reduced diameter section with an integral flattened ridge. The flow of combustion gases through the heat exchanger tubes may be partially constricted inside the reduced diameter sections. When installed in an HVAC system the integral flattened ridges may be angled to intercept the flow of air outside the heat exchanger tubes.

First claim

What is claimed is:

1. A heat exchange tube comprising:
a standard diameter section comprising a largest diameter; and
at least one reduced diameter section comprising a reduced circumference and an integral flattened ridge, the integral flattened ridge extending outwardly from the reduced circumference and past the largest diameter of the heat exchange tube.

2. The heat exchange tube of claim 1 , additionally comprising an upper straight section, a lower straight section, and a bent section connecting the upper straight section with the lower straight section, wherein the upper straight section and the lower straight section are about parallel to each other.

3. The heat exchange tube of claim 1 , wherein the integral flattened ridge extends along a portion of a length of the at least one reduced diameter section.

4. The heat exchange tube of claim 1 , wherein the heat exchange tube is straight.

5. The heat exchange tube of claim 1 , wherein the heat exchange tube comprises between 2-8 reduced diameter sections.

6. The heat exchange tube of claim 5 , wherein a length of one of the reduced diameter sections is different from a length of at least one other reduced diameter section.

7. The heat exchange tube of claim 5 , wherein the heat exchange tube comprises 5 reduced diameter sections.

8. The heat exchange tube of claim 1 , wherein the at least one reduced diameter section has a diameter that is about less than two thirds the largest diameter of the heat exchange tube.

9. The heat exchange tube of claim 8 , wherein the at least one reduced diameter section has a diameter that is about half the diameter of the largest diameter of the heat exchange tube.

10. The heat exchange tube of claim 1 , wherein the integral flattened ridge extends past the largest diameter of the heat exchange tube by at least 20 percent of the largest diameter of the heat exchange tube.

11. The heat exchange tube of claim 1 , wherein a working fluid is able to move within the flattened ridge.

12. The heat exchange tube of claim 2 , wherein the integral flattened ridge extends at an angle of between −90 degrees and 90 degrees from a direction of air flow over the heat exchange tube.

13. A furnace comprising:
a heat exchanger comprising a plurality of heat exchange tubes,
wherein the plurality of heat exchange tubes are configured to receive a working fluid from a burner assembly, and
wherein each heat exchange tube comprises:
a standard diameter section comprising a largest diameter, and
a reduced diameter section comprising a reduced circumference and an integral flattened ridge, the integral flattened ridge extending outwardly from the reduced circumference and past the largest diameter of the heat exchange tube;

an exhaust configured to receive the working fluid from the plurality of heat exchange tubes; and
a circulation blower fan configured to move air over an outside of the plurality of heat exchange tubes and into a supply duct.

14. The furnace of claim 13 , wherein the integral flattened ridge extends at an angle of between −90 degrees and 90 degrees from a direction of air flow through the heat exchanger.

15. The furnace of claim 13 , wherein the heat exchanger comprises between 2-20 heat exchange tubes.

16. The furnace of claim 14 , wherein each heat exchange tube comprises between 2-8 reduced diameter sections with integral flattened ridges.

17. The furnace of claim 13 , wherein the integral flattened ridge extends at an angle of between −90 to −60 or 60 to 90 degrees from a direction of air flow through the heat exchanger.

18. The furnace of claim 13 , wherein each heat exchange tube additionally comprises an upper straight section, a lower straight section, and a bent section connecting the upper straight section with the lower straight section, wherein the upper straight section and the lower straight section are about parallel to each other.

19. The furnace of claim 18 , wherein the upper straight section and the lower straight section define a reference plane that forms an angle between −90° to 90° from a direction of air flow through the heat exchanger.

Assignees

• Rheem Mfg Co

Inventors

• Kanagala Hari Krishna
• Frederick Ken
• Binz Darrell

Classifications

• F24D2220/06

  Heat exchangers · CPC title

• F28F1/006 Primary

  with variable shape, e.g. with modified tube ends, with different geometrical features (F28F1/025, F28F1/06, F28F1/08, F28F9/16, F28F9/18 take precedence) · CPC title

• F28F13/08

  by varying the cross-section of the flow channels · CPC title

• F24H3/087

  using fluid fuel · CPC title

• F28F2001/027

  with dimples · CPC title