IP Library Granted Patent US 6,959,758
Granted Patent B2
US 6,959,758 · App. 10/308,304 · Granted Nov 1, 2005

Serpentine tube, cross flow heat exchanger construction

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 6,959,758
App. No.
10/308,304
Granted
Nov 1, 2005
Kind
B2
Abstract

A heat exchanger ( 10 ) is provided to transfer heat between a first and second fluid flow. The heat exchanger 10 includes a flow path ( 20 ) provided in the form of one or more heat exchange tubes ( 40, 40 A-C), and a second flow path ( 30 ) provided in the form of one or more serpentine heat exchange tubes ( 42, 42 A-C). The tube(s) ( 40, 40 A-C) is (are) “woven” together with the tube(s) ( 42, 42 A-C) such that they are perpendicular to each other. The heat exchanger ( 10 ) can provide particular advantages when used as a suction line heat exchanger in a transcritical cooling system ( 12 ).

Claims (33)

1. A heat exchanger for transferring heat between first and second fluid flows, the heat exchanger comprising:

a plurality of flattened, first heat exchange tubes to direct the first fluid flow through the heat exchanger, each first tube including at least a first pair of substantially parallel, spaced tube runs connected by a bend in the first tube, the first pairs of tube runs being substantially aligned with each other;

a plurality of flattened, second heat exchange tubes to direct the second fluid flow through the heat exchanger, each second tube including at least a second pair of substantially parallel, spaced tube runs connected by a bend in the second tube, the second pairs of tube runs being substantially aligned with each other and substantially perpendicular to the first pairs of tube runs;

one of the tube runs of each of the second tubes being sandwiched between the tube runs of each first pair of tube runs of the first tubes, and

one of the tube runs of each of the first tubes being sandwiched between the tube runs of each second pair of tube runs of the second tubes.

2. The heat exchanger of claim 1 further wherein:

each of said second tubes includes an additional tube run substantially parallel to the second pair of tube runs of the second tube and connected to said one of the tube runs of the second tube by an additional bend; and

the other one of the tube runs of each of the first tubes is sandwiched between the additional tube run of each of the second tubes and said one of the tube runs of each of the second tubes.

3. The heat exchanger of claim 1 further comprising:

a first pair of manifolds connected to opposite ends of each of the first tubes to collect the first fluid from and distribute the first fluid to the first tubes; and

a second pair of manifolds connected to opposite ends of each of the second tubes to collect the second fluid from and distribute the second fluid to the second tubes.

4. A heat exchanger for transferring heat between first and second fluid flows, the heat exchanger comprising:

a plurality of first heat exchange tubes to direct the first fluid flow through the heat exchanger, each first tube including at least a first pair of substantially parallel, spaced tube runs connected by a bend in the first tube, the first pairs of tube runs being substantially aligned with each other;

a plurality of second heat exchange tubes to direct the second fluid flow through the heat exchanger, each second tube including at least three substantially parallel, spaced tube runs connected by bends in the second tube, the tube runs of each of the second tubes being substantially aligned with the tube runs of the other of the second tubes and substantially perpendicular to the first pairs of tube runs;

one of the tube runs of each of the second tubes being sandwiched between the tube runs of each first pair of tube runs of the first tubes;

one of the tube runs of each of the first tubes being sandwiched between said one of the tube runs of each of the second tubes and another of the tube runs of each of the second tubes; and

the other of the tube runs of each of the first tubes being sandwiched between another of the tube runs of each of the second tubes and said one of the tube runs of each of the second tubes.

5. The heat exchanger of claim 4 further wherein each of the first and second tubes is a flattened tube.

6. The heat exchanger of claim 4 further comprising:

a first pair of manifolds connected to opposite ends of each of the first tubes to collect the first fluid from and distribute the first fluid to the first tubes; and

a second pair of manifolds connected to opposite ends of each of the second tubes to collect the second fluid from and distribute the second fluid to the second tubes.

7. A heat exchanger for use in a transcritical cooling system including a compressor, a gas cooler that receives a high pressure refrigerant flow from the compressor and delivers a cooled high pressure refrigerant to the system, an expansion device that receives the high pressure refrigerant flow from the gas cooler and delivers a low pressure refrigerant flow to the system, and an evaporator that receives the low pressure refrigerant flow and delivers heated low pressure refrigerant to the system, the heat exchanger comprising:

a first inlet manifold adapted to receive the high pressure refrigerant flow from the system;

a plurality of flattened, first heat exchange tubes connected to the first inlet manifold to receive the high pressure refrigerant therefrom, each first tube including at least a first pair of substantially parallel, spaced tube runs connected by a bend in the first tube, the first pairs of tube runs being substantially aligned with each other;

a first outlet manifold connected to the first tubes to collect the high pressure refrigerant flow therefrom;

a second inlet manifold adapted to receive the low pressure refrigerant flow from the system;

a plurality of flattened, second heat exchange tubes to direct the second fluid through the heat exchanger, each second tube including at least a second pair of substantially parallel, spaced tube runs connected by a bend in the second tube, the second pairs of tube runs being substantially aligned with each other and substantially perpendicular to the first pairs of tube runs; and

a second outlet manifold connected to the second tubes to collect the low pressure refrigerant flow therefrom; wherein

one of the tube runs of each of the second tubes is sandwiched between the tube runs of each first pair of tube runs of the first tubes, and

one of the tube runs of each of the first tubes is sandwiched between the tube runs of each second pair of tube runs of the second tube.

8. The heat exchanger of claim 7 further wherein:

each of said second tubes includes an additional tube run substantially parallel to the second pair of tube runs of the second tube and connected to said one of the tube runs of the second tube by an additional bend; and

the other one of the tube runs of each of the first tubes is sandwiched between the additional tube run of each of the second tubes and said one of the tube runs of each of the second tubes.

Assignments (2)
SECURITY AGREEMENT Recorded Feb 18, 2009
From: MODINE MANUFACTURING COMPANY; MODINE, INC.; MODINE ECD, INC.
To: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT
Reel/Frame 022266/0552 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 3, 2004
From: HUGHES, GREGORY G.; MEMORY, STEPHEN
To: MODINE MANUFACTURING COMPANY
Reel/Frame 015638/0516 →