# US 10,502,493 B2 · Single pass cross-flow heat exchanger

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- Number: US 10,502,493 B2
- Document ID: US10502493B2
- Status: Granted
- Kind: B2
- Application number: 15/358,310
- Filed: 2016-11-22
- Published: 2018-05-24
- Granted: 2019-12-10
- Earliest claimed: 2016-11-22
- Assignees: General Electric Company
- Applicants: General Electric Company
- Inventors: Sebastian Walter Freund
- Web page: https://patentgrep.com/patent/US10502493B2

## CPC

- F28D 1/0435: {Combination of units extending one behind the other (F28D1/0452 takes precedence)}
- F28B 1/06: using air or other gas as the cooling medium
- F28D 1/05308: {Assemblies of conduits connected side by side or with individual headers, e.g. section type radiators (F28D1/05358 takes precedence)}
- F28D 1/05341: {with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators}
- F28D 21/0014: {the heat being recuperated from waste air or from vapors (for air conditioning F24F12/001)}
- F28F 1/12: the means being only outside the tubular element
- F28F 1/24: and extending transversely (F28F1/38 takes precedence)
- F28D 2021/0026: {for combustion engines, e.g. for gas turbines or for Stirling engines}
- F28D 2021/0064: {Vaporizers, e.g. evaporators}
- F28F 2250/106: with cross flow
- F28D: HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT (fluid heaters having heat generating means and heat transferring means F24H; furnaces F27; details of heat-exchange apparatus of general)
- F28B: STEAM OR VAPOUR CONDENSERS (condensation of vapours B01D5/00; steam engine plants having condensers F01K; liquefaction of gases F25J; details of heat-exchange and heat-transfer arrangements of general application F28F)
- F28F: DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION (water and air traps, air venting F16)

## Abstract

The present application provides a heat exchanger for exchanging heat between two fluid flows in cross-flow arrangement. The heat exchanger includes at least one heat exchanging module including a first heat exchanging component and a second heat exchanging component. The first heat exchanging component including a fluid inlet header, a fluid outlet header, and at least one heat exchanging passageway defining a first tube-side fluid flow path of a first portion of a fluid in a first direction. The second heat exchanging component including a fluid inlet header, a fluid outlet header, and at least one heat exchanging passageway defining a second tube-side fluid flow path in a second direction for an additional portion of the fluid, wherein the first direction is opposed to the second direction. The opposing first tube-side fluid flow path and the second tube-side fluid flow path equalizing the temperature distribution over the cross-section of a cross-flow fluid exiting the module.

## Claims

### Claim 1

A heat exchanger for exchanging heat between two fluid flows in cross-flow arrangement and having improved temperature distribution, comprising:
at least one heat exchanging module disposed to receive a fluid and in a cross-flow fluid path configuration with a cross-flow fluid, each heat exchanging module comprising a first heat exchanging component and a second heat exchanging component;
the first heat exchanging component comprising a first fluid inlet header for input of a portion of the fluid, a first fluid outlet header for output of the portion of the fluid, and at least one first heat exchanging passageway disposed therebetween and defining a first tube-side fluid flow path in a first direction, perpendicular to the cross-flow fluid path, for the portion of the fluid; and
the second heat exchanging component comprising a second fluid inlet header for input of a remaining portion of the fluid, a second fluid outlet header for output of the remaining portion of the fluid, and at least one second heat exchanging passageway disposed therebetween and defining a second tube-side fluid flow path in a second direction, perpendicular to the cross-flow fluid path and parallel to the first tube-side fluid flow path, for the remaining portion of the fluid, wherein the first direction is opposite the second direction,
wherein the opposing first tube-side fluid flow path and the second tube-side fluid flow path equalize a temperature distribution over a cross-section of the cross-flow fluid exiting the at least one heat exchanging module.

### Claim 2 (depends on 1)

The heat exchanger of claim 1, wherein the heat exchanger includes a plurality of heat exchanging modules disposed in one of a serial arrangement or a parallel arrangement with respect to the first tube-side fluid flow and the second tube-side fluid flow and a serial arrangement with respect to the second, cross-flow fluid.

### Claim 3 (depends on 1)

The heat exchanger of claim 1, wherein at least one of the at least one first heat exchanging passageway or the at least one second heat exchanging passageway in the at least one heat exchanging module comprise a plurality of heat exchanging tubes including a plurality of fins disposed thereon, the plurality of fins spaced from each other in parallel and allowing the second, cross-flow fluid to pass through a gap therebetween.

### Claim 4 (depends on 3)

The heat exchanger of claim 3, wherein the plurality of fins on each of the plurality of heat exchanging tubes are designed with a fin height and a fin density to provide one of a minimum heat exchanging tube temperature or a maximum heat exchanging tube temperature relative to a total amount of heat exchanged and equalize a temperature distribution of a tube-side fluid exiting the plurality of heat exchanging tubes.

### Claim 5 (depends on 1)

The heat exchanger of claim 1, wherein the portion of the fluid as a first tube-side fluid flow is guided from the first fluid inlet header of the first heat exchanging component, through the at least one first heat exchanging passageway of the first heat exchanging component, and passes out of the first fluid outlet header of the first heat exchanging component, and wherein the remaining portion of the fluid as a second tube-side fluid flow is guided from the second fluid inlet header of the second heat exchanging component, through the at least one second heat exchanging passageway of the second heat exchanging component in the second direction opposing that of the first tube-side fluid flow, and passes out of the second fluid outlet header of the second heat exchanging component.

### Claim 6 (depends on 5)

The heat exchanger of claim 5, wherein the first tube-side fluid flow and the second tube-side fluid flow are a high-pressure fluid flow and wherein the second, cross-flow fluid is a low-pressure fluid flow.

### Claim 7 (depends on 5)

The heat exchanger of claim 5, wherein the first tube-side fluid flow and the second tube-side fluid flow are one of a vapor or gas and wherein the second, cross-flow fluid is low-pressure air.

### Claim 8 (depends on 1)

The heat exchanger of claim 1, wherein the plurality of heat exchanging passageways of the first heat exchanging component and the second heat exchanging component have similar dimensions, shapes, lengths, diameters, circumferences, sizes, or combinations thereof.

### Claim 9 (depends on 1)

The heat exchanger of claim 1, wherein the heat exchanger is mounted along an exhaust gas duct.

### Claim 10 (depends on 9)

The heat exchanger of claim 9, wherein the heat exchanger is disposed in the exhaust gas duct whereby the plurality of heat exchanging passageways of the first heat exchanging component and the second heat exchanging component are in a perpendicular configuration with respect to a direction of flow of an exhaust gas that composes the second, cross-flow fluid.

### Claim 11 (depends on 1)

The heat exchanger of claim 1, wherein the heat exchanger comprises an air-cooled heat exchanger.
