Heat exchangers

Patent metadata

Field	Value
Publication number	US-10697708-B2
Application number	US-201715489964-A
Country	US
Kind code	B2
Filing date	Apr 18, 2017
Priority date	Apr 18, 2016
Publication date	Jun 30, 2020
Grant date	Jun 30, 2020

Abstract

A plate fin heat exchanger comprises a circular section tubular shell. The shell comprises a plurality of first shell openings arranged along a length of the shell and a plurality of second shell openings arranged along a length of the shell. A first fluid plenum is provided on the shell in fluid communication with the first shell openings. A second fluid plenum is provided on the shell in fluid communication with the second shell openings. The heat exchanger further comprises a core extending axially within the tubular shell. The core comprises an axially extending first core passage and a second axially extending core passage isolated from the first core passage.

First claim

The invention claimed is:

1. A heat exchanger comprising:
a circular section tubular shell comprising:
a plurality of first shell openings arranged along a length of the circular section tubular shell;
a plurality of second shell openings arranged along a length of the circular section tubular shell;
a first fluid plenum provided on the circular section tubular shell in fluid communication with the first shell openings;

a second fluid plenum provided on the circular section tubular shell in fluid communication with the second shell openings;
a core extending axially within the circular section tubular shell and comprising:
an axially extending first core passage and an axially extending second core passage isolated from the first core passage, the first core passage comprising a plurality of first core openings and the second core passage comprising a plurality of second core openings; and
a plurality of thermally conductive plates mounted between the circular section tubular shell and the core to form a plurality of adjacent first and second flow passages between the core and the circular section tubular shell;
wherein respective first shell openings and first core openings open into respective first flow passages and respective second shell openings and second core openings open into respective second flow passages to conduct the respective first and second fluids between the core and the shell.

2. The heat exchanger as claimed in claim 1 , wherein the first and second shell openings are arranged in circumferentially offset rows along the circular section tubular shell and the first and second core openings are arranged in circumferentially offset rows along the core.

3. The heat exchanger as claimed in claim 1 , wherein the first and second shell openings are axially offset from one another and the first and second core openings are axially offset from one another.

4. The heat exchanger as claimed in claim 1 , wherein respective first shell and first core openings are radially aligned and respective second shell and second core openings are radially aligned.

5. The heat exchanger as claimed in claim 1 , further comprising one or more flow blocking elements arranged in each flow passage between adjacent plates for blocking direct flow between the shell openings and core openings.

6. The heat exchanger as claimed in claim 1 , further comprising one or more baffles arranged in each flow passage between adjacent plates for creating a tortuous flow path between the core openings and the shell openings.

7. The heat exchanger as claimed in claim 6 , comprising one or more baffles extending outwardly from the core and one or more baffles extending inwardly from the circular section tubular shell.

8. The heat exchanger as claimed in claim 5 , wherein the at least one flow blocking element or baffle is attached to and spaces adjacent plates.

9. The heat exchanger as claimed in claim 1 , comprising one or more fin elements arranged in the first and second flow passages.

10. The heat exchanger as claimed in claim 9 , wherein the at least one fin element is a corrugated, perforated or serrated element.

11. The heat exchanger as claimed in claim 9 , wherein the at least one fin element is an annular element.

12. The heat exchanger as claimed in claim 9 , wherein the at least one fin element comprises at least one slot for receiving the at least one flow blocking element or baffle.

13. The heat exchanger as claimed in claim 1 , wherein the core comprises a tube with an internal partition to form the first and second fluid passages.

14. The heat exchanger as claimed in claim 1 , comprising a connector block at one end of the circular section tubular shell having passages for conducting the first and second fluids to and away from the core passages and the circular section tubular shell plenums.

15. The heat exchanger as claimed in claim 14 , wherein the connector block comprises a pressure relief valve arranged in a bypass passage between a core passage inlet and a shell plenum outlet, the pressure relief valve operable to open to allow flow through the bypass passage when a fluid pressure exceeds a predetermined maximum value.

Assignees

• Hamilton Sundstrand Corp
• Hamilton Sunstrand Corp

Inventors

• Lewandowski Rafal

Classifications

• F28F9/026 Primary

  with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits · CPC title

• F28D9/0006

  the plate-like or laminated conduits being enclosed within a pressure vessel · CPC title

• F28F2009/228

  Oblique partitions · CPC title

• F28D9/0012

  the apparatus having an annular form · CPC title

• F28F2009/226

  Transversal partitions · CPC title