# US 12,007,176 B2 · Heat exchanger and method of manufacturing a heat exchanger

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- Number: US 12,007,176 B2
- Document ID: US12007176B2
- Status: Granted
- Kind: B2
- Application number: 16/023,478
- Filed: 2018-06-29
- Published: 2019-01-31
- Granted: 2024-06-11
- Earliest claimed: 2016-03-30
- Assignees: Woodside Energy Technologies Pty Ltd
- Applicants: Woodside Energy Technologies Pty Ltd
- Inventors: Geoffrey Byfield
- Web page: https://patentgrep.com/patent/US12007176B2

## CPC

- F28D 7/0008: {the conduits for one medium being in heat conductive contact with the conduits for the other medium}
- B22F 5/10: of articles with cavities or holes, not otherwise provided for in the preceding subgroups
- B22F 10/20: Direct sintering or melting
- B33Y 80/00: Products made by additive manufacturing
- F28D 9/0025: {the conduits being formed by zig-zag bend plates}
- F28D 9/0037: {the conduits for the other heat-exchange medium also being formed by paired plates touching each other (F28D9/0043 takes precedence)}
- F28D 9/0062: {the conduits for one heat-exchange medium being formed by spaced plates with inserted elements (F28D9/0012, F28D9/0025, F28D9/0081, F28D9/04 take precedence)}
- F28F 3/086: {having one or more openings therein forming tubular heat-exchange passages}
- F28F 7/02: Blocks traversed by passages for heat-exchange media {(F28D7/0008 takes precedence)}
- F28F 2255/18: sintered
- Y02P 10/25: Process efficiency
- 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)
- B22F: WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER (making alloys by powder metallurgy C22C); APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B33Y: ADDITIVE MANUFACTURING, i.e. MANUFACTURING OF THREE-DIMENSIONAL [3D] OBJECTS BY ADDITIVE DEPOSITION, ADDITIVE AGGLOMERATION OR ADDITIVE LAYERING, e.g. BY 3D PRINTING, STEREOLITHOGRAPHY OR SELECTIVE LASER SINTERING
- F28F: DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION (water and air traps, air venting F16)
- Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS

## Abstract

A heat exchanger includes a plurality of sets of fluid channels, each fluid channel including first and second end portions and an intermediate portion between the first and second end portions. The first end portions in a plane perpendicular to a direction of fluid flow in the channels have respective end perimeters which are in a first configuration, where adjacent end portions of different sets of fluid channels have a total first shared heat transfer length, this being a summation of lengths of mutually opposed perimeters of the so adjacent end portions of the different sets. The intermediate portions of the channels in a plane transverse to the direction of fluid flow have respective intermediate channel perimeters, the intermediate portions having a second configuration with a total second shared heat transfer length being a summation of lengths of mutually opposed channel perimeters of the adjacent channels of the different sets. Therefore, the total second shared heat transfer length is different to, and moreover greater than, the total first heat transfer length.

## Claims

### Claim 1

A heat exchanger comprising:
at least a first set of fluid channels and a second set of fluid channels, each fluid channel of the first and second sets of fluid channels having a first end portion, a second end portion, and an intermediate portion between the first and second end portions;
the first end portions and the second end portions being arranged in alternating planes of channels so that each plane contains only fluid channels from the same set of fluid channels; and
a first transition zone, a second transition zone and a heat transfer zone between the first and second transition zones;
wherein:
the first end portions extend through the first transition zone, the second end portions extend through the second transition zone, and the intermediate portions extend through the heat transfer zone;
the first transition zone includes one or more groups of fluid channels, wherein each group of fluid channels comprises:
at least one fluid channel of the first set and at least one fluid channel of the second set;
less fluid channels of the first set than a number of fluid channels in any one of the planes of fluid channels of the first set; and
less fluid channels of the second set than a number of fluid channels in any one of the planes of fluid channels of the second set; and
the one or more groups of fluid channels are rotated about respective axes parallel to a direction of flow of fluid through the fluid channels through 180° relative to other non-rotated fluid channels so that, when the channels reach and extend through the heat transfer zone, the fluid channels of the first and second sets are arranged in a chequer board configuration formed of rotated and non-rotated fluid channels.

### Claim 2 (depends on 1)

The heat exchanger of claim 1, wherein each group of fluid channels comprises a single fluid channel from the first set of fluid channels and a single fluid channel from the second set of fluid channels.

### Claim 3 (depends on 1)

The heat exchanger of claim 1, wherein each fluid channel defines a fluid flow path through the heat exchanger extending from the first end portion to the second end portion and wherein the transition zone extends for at least one quarter of the length of the fluid flow path through the heat exchanger.

### Claim 4 (depends on 1)

The heat exchanger of claim 1, wherein each fluid channel has a constant cross-sectional shape from the first end portion to the second end portion, wherein the cross-sectional shape is viewed perpendicular to the direction of flow of fluid through the heat exchanger.

### Claim 5 (depends on 4)

The heat exchanger of claim 4, wherein the cross-sectional shape is selected from the group consisting of a circle, an ellipse, and a rounded polygon with four or more sides.

### Claim 6 (depends on 1)

The heat exchanger of claim 1, wherein an internal surface of the at least one fluid channel in at least one of the sets of fluid channels is arranged to induce turbulence in fluid when flowing through the at least one fluid channel.

### Claim 7 (depends on 6)

The heat exchanger of claim 6, wherein the internal surface of the at least one fluid channel is one, or a combination of any two or more, of: (a) roughened, (b) provided with one or more grooves, (c) provided with one or more protruding ridges or ribs, (d) provided with raised dimples, and (e) provided with one or more fins, to induce turbulence in a fluid when flowing through the at least one channel.

### Claim 8

A heat exchanger comprising:
at least a first set of fluid channels and a second set of fluid channels, each fluid channel of the first set of fluid channels and second set of fluid channels having a first end portion, a second end portion, and an intermediate portion between the first and second end portions;
the first end portions and the second end portions being arranged in alternating planes of fluid channels so that each plane contains only fluid channels from the same set of fluid channels;
a first transition zone, a second transition zone and a heat transfer zone between the first and second transition zones;
wherein:
the first end portions extend through the first transition zone, the second end portions extend through the second transition zone, and the intermediate portions extend through the heat transfer zone; and
the first transition zone includes a plurality of fluid channels provided within corresponding rotating groups that rotate the fluid channels within each rotating group between the first transition zone and the heat transfer zone, wherein, in the first transition zone:
a first rotating group of fluid channels comprises one fluid channel of the first set of fluid channels and one fluid channel of the second set of fluid channels;
a second rotating group of fluid channels comprises one fluid channel of the first set of fluid channels and one fluid channel of the second set of fluid channels, the second rotating group of fluid channels being adjacent to the first rotating group of fluid channels;
at least one of the first rotating group of fluid channels and the second rotating group of fluid channels rotates about a respective axis that is parallel to a direction of flow of fluid through the fluid channels; and
each fluid channel that rotates between the first transition zone and the heat transfer zone is provided within a single rotating group such that, when the first set of fluid channels and the second set of fluid channels reach and extend through the heat transfer zone, the first set of fluid channels and the second set of fluid channels are arranged in a chequer board configuration.

### Claim 9 (depends on 8)

The heat exchanger of claim 8, wherein each fluid channel defines a fluid flow path through the heat exchanger extending from the first end portion to the second end portion and wherein the transition zone extends for at least one quarter of the length of the fluid flow path through the heat exchanger.

### Claim 10 (depends on 8)

The heat exchanger of claim 8, wherein each fluid channel has a constant cross-sectional shape from the first end portion to the second end portion, wherein the cross-sectional shape is viewed perpendicular to the direction of flow of fluid through the heat exchanger.

### Claim 11 (depends on 10)

The heat exchanger of claim 10, wherein the cross-sectional shape is selected from the group consisting of a circle, an ellipse, and a rounded polygon with four or more sides.

### Claim 12 (depends on 8)

The heat exchanger of claim 8, wherein an internal surface of the at least one fluid channel in at least one of the sets of fluid channels is arranged to induce turbulence in fluid when flowing through the at least one fluid channel.

### Claim 13 (depends on 12)

The heat exchanger of claim 12, wherein the internal surface of the at least one fluid channel is one, or a combination of any two or more, of: (a) roughened, (b) provided with one or more grooves, (c) provided with one or more protruding ridges or ribs, (d) provided with raised dimples, and (e) provided with one or more fins, to induce turbulence in a fluid when flowing through the at least one fluid channel.