Flat-tubed heat exchanger

• US 5,826,646 A
• Filed: 07/02/1997
• Issued: 10/27/1998
• Est. Priority Date: 10/26/1995
• Status: Expired due to Term

• Current Assignee: Heatcraft Incorporated (Lennox International Incorporated)
• Original Assignee: Heatcraft Incorporated (Lennox International Incorporated)
• Inventors: Heidenreich, Michael E., Bae, Young L.
• Primary Examiner(s): Leo, Leonard R.
• Application Number:
  US08/887,092
• Time in Patent Office: 482 Days
• Field of Search: 165/170, 165/153, 165/177, 165/178, 165/183, 165/110, 29/890.046, 29/890.049
• US Class Current: 165/110
• CPC Class Codes: F25B 39/02 Evaporators
• CPC Class Codes: F25B 39/04 Condensers
• CPC Class Codes: F28D 1/0308 the conduits being formed by paired plates touching each other F28D1/0358 takes precedence
• CPC Class Codes: F28D 2021/0084 Condensers
• CPC Class Codes: F28D 2021/0085 Evaporators
• CPC Class Codes: F28F 3/04 the means being integral with the element

Abstract

A heat exchanger with an improved flat-tubed design is disclosed. The heat exchanger includes plural tubes of relatively flat cross-section in parallel array. Each tube is comprised of relatively flat first and second plates in facing contact. The first plate of each tube has a plurality of first grooves extending at a first oblique angle with respect to a major axis of the corresponding tube. The second plate of each tube has a plurality of second grooves extending at a second oblique angle with respect to the major axis of the corresponding tube, such that the first and second grooves define a cross-hatched pattern of channels to accommodate flow of heat transfer fluid through the corresponding tube. The first grooves are defined by corresponding first ridges on a first major surface of the first plate and the second grooves are defined by corresponding second ridges on a second major surface of the second plate. The first and second major surfaces are in facing relationship and each of the first ridges is in contact with at least one of the second ridges. The first grooves are located above the second grooves. When the heat transfer fluid consists of fluid in both liquid and vapor states, the heavier liquid will tend to flow through the second grooves while the lighter vapor will tend to flow through the first grooves. Because the first grooves extend in a different direction from the second grooves, separation between the liquid and vapor within the tubes is enhanced.

Claims

1. In a cooling system, a heat exchanger for condensing a vapor compression refrigerant in said heat exchanger by transferring heat from the refrigerant to an external fluid flowing through said heat exchanger, said heat exchanger comprising:

a pair of spaced headers, one of said headers having a refrigerant inlet and one of said headers having a refrigerant outlet; and

an elongated tube of non-circular cross-section extending between said headers and in fluid communication therewith at respective opposed ends of said tube, said tube having opposed top and bottom portions and opposed first and second sides, said top portion having a plurality of first grooves in parallel array extending in a first direction toward said first side and at a first oblique angle with respect to a central longitudinal axis of said tube, said bottom portion having a plurality of second grooves in parallel array extending in a second direction toward said second side and at a second oblique angle with respect to said central longitudinal axis, said first grooves being in crossing relationship with said second grooves to define a cross-hatched pattern of channels to accommodate refrigerant flow through said tube, said tube being tilted about the central longitudinal axis thereof such that said first side is higher than said second side, whereby separation between refrigerant in a vapor state and refrigerant in a liquid state is enhanced within said tube, said first side being a leading side of said tube such that the external fluid flowing through said heat exchanger first encounters said first side.

2. The heat exchanger of claim 1 wherein each of said tubes has a generally rectangular cross-section.

3. The heat exchanger of claim 1 wherein said first oblique angle and said second oblique angle are in a range from 20°

to 45°

with respect to said central longitudinal axis.

4. The heat exchanger of claim 1 wherein said top portion is comprised of a top plate and said bottom portion is comprised of a bottom plate, said top plate having a first major surface and said bottom plate having a second major surface in facing relationship with said first major surface, said first major surface having plural first ridges in parallel array extending in said first direction and said second major surface having plural second ridges in parallel array extending in said second direction, each of said first ridges being in contact with at least one of said second ridges, each of said first grooves being defined by two adjacent first ridges and each of said second grooves being defined by two adjacent second ridges.

5. The heat condenser of claim 4 wherein each of said first ridges and each of said second ridges have a generally trapezoidal cross-section.

6. The heat exchanger of claim 4 wherein each of said first ridges and each of said second ridges have a generally triangular cross-section.

7. The heat exchanger of claim 4 wherein said central longitudinal axis extends generally horizontally between said headers, said tube being tilted such that an axis extending perpendicularly through said first and second major surfaces is offset from a vertical axis with an acute angle therebetween.

8. In a cooling system, a heat exchanger for evaporating a vapor compression refrigerant in said heat exchanger by transferring heat to the refrigerant from an external fluid flowing through said heat exchanger, said heat exchanger comprising:

a pair of spaced headers, one of said headers having a refrigerant inlet and one of said headers having a refrigerant outlet; and

an elongated tube of non-circular cross-section extending between said headers and in fluid communication therewith at respective opposed ends of said tube, said tube having opposed top and bottom portions and opposed first and second sides, said top portion having a plurality of first grooves in parallel array extending in a first direction toward said first side and at a first oblique angle with respect to a central longitudinal axis of said tube, said bottom portion having a plurality of second grooves in parallel array extending in a second direction toward said second side and at a second oblique angle with respect to said central longitudinal axis, said first grooves being in crossing relationship with said second grooves to define a cross-hatched pattern of channels to accommodate refrigerant flow through said tube, said tube being tilted about the central longitudinal axis thereof such that said second side is higher than said first side, whereby mixing between refrigerant in a vapor state and refrigerant in a liquid state is enhanced within said tube, said second side being a leading side of said tube such that the external fluid flowing through said heat exchanger first encounters said second side.

9. The heat exchanger of claim 8 wherein said tube has a generally rectangular cross-section.

10. The heat exchanger of claim 8 wherein said first oblique angle and said second oblique angle are in a range from 20°

to 45°

with respect to said central longitudinal axis.

11. The heat exchanger of claim 8 wherein said top portion is comprised of a top plate and said bottom portion is comprised of a bottom plate, said top plate having a first major surface and said bottom plate having a second major surface in facing relationship with said first major surface, said first major surface having plural first ridges in parallel array extending in said first direction and said second major surface having plural second ridges in parallel array extending in said second direction, each of said first ridges being in contact with at least one of said second ridges, each of said first grooves being defined by two adjacent first ridges and each of said second grooves being defined by two adjacent second ridges.

12. The heat exchanger of claim 11 wherein each of said first ridges and each of said second ridges have a generally trapezoidal cross-section.

13. The heat exchanger of claim 11 wherein each of said first ridges and each of said second ridges have a generally triangular cross-section.

14. The heat exchanger of claim 11 wherein said central longitudinal axis extends generally horizontally between said headers, said tube being tilted such that an axis extending perpendicularly through said first and second major surfaces is offset from a vertical axis with an acute angle therebetween.

15. In a cooling system, a heat exchanger for condensing a vapor compression refrigerant in said heat exchanger by transferring heat from the refrigerant to an external fluid flowing through said heat exchanger, said heat exchanger comprising:

a pair of spaced headers, one of said headers having a refrigerant inlet and one of said headers having a refrigerant outlet, each of said headers being in an upright, vertically oriented position; and

an elongated tube of non-circular cross-section extending between said headers and in fluid communication therewith at respective opposed ends of said tube, said tube having opposed top and bottom portions and opposed first and second sides, said top portion having a plurality of first grooves in parallel array extending in a first direction toward said first side and at a first oblique angle with respect to central longitudinal axis of said tube, said bottom portion having a plurality of second grooves in parallel array extending in a second direction toward said second side and at a second oblique angle with respect to said central longitudinal axis, said first grooves being in crossing relationship with said second grooves to define a cross-hatched pattern of channels to accommodate refrigerant flow through said tube, said tube being tilted about the central longitudinal axis thereof such that said first side is higher than said second side, whereby separation between refrigerant in a vapor state and refrigerant in a liquid state is enhanced within said tube, said first side being a leading side of said tube such that the external fluid flowing through said heat exchanger first encounters said first side.

16. The heat exchanger of claim 15 wherein said first oblique angle and said second oblique angle are in a range from 20°

to 45°

with respect to said central longitudinal axis.

17. The heat exchanger of claim 15 wherein said tube is comprised of top and bottom plates, said top plate defining said top portion of said tube and said bottom plate defining said bottom portion of said tube, said top plate having a first major surface and said bottom plate having a second major surface in facing relationship with said first major surface, said first major surface having plural first ridges in parallel array extending in said first direction, said second major surface having plural second ridges in parallel array extending in said second direction, each of said ridges being in contact with at least one of said second ridges, each of said first grooves being defined by two adjacent first ridges and each of said second grooves being defined by two adjacent second ridges.

18. The heat exchanger of claim 17 wherein each of said first ridges and each of said second ridges have a generally trapezoidal cross-section.

19. The heat exchanger of claim 17 wherein each of said first ridges and each of said second ridges have a generally triangular cross-section.

20. The heat exchanger of claim 17 wherein said central longitudinal axis extends generally horizontally between said headers, said tube being tilted such that an axis extending perpendicularly through said first and second major surfaces is offset from a vertical axis with an acute angle therebetween.