Multi-zone shell and tube heat exchanger

Patent metadata

Field	Value
Publication number	US-11353266-B2
Application number	US-202017036392-A
Country	US
Kind code	B2
Filing date	Sep 29, 2020
Priority date	Sep 29, 2020
Publication date	Jun 7, 2022
Grant date	Jun 7, 2022

Abstract

A shell and tube heat exchanger has elongated shell having first and second opposing ends and an open interior. A core divides the open interior of the shell into first and second enclosed portions. The shell has first and second tube fluid openings at opposing ends. End plates divide the first and second enclosed portions into manifold portions and enclosed shell chamber portions. Tubes extend from the end plates, through the enclosed shell chambers to the core. Shell fluid openings are at sides of the elongated shell, a first fluid opening communicating with the first shell chamber, and a second fluid opening communicating with the second shell chamber. The shell has a long axis, and the end plates are angled relative to the long axis. The tubes are polygonal with rounded corners and straight sides. The heat exchanger can be used for both evaporation and condensation processes.

First claim

We claim:

1. A shell and tube heat exchanger, comprising:
an elongated shell having first and second opposing ends and an open interior; a core dividing the open interior of the shell into first and second enclosed portions; a first tube fluid opening at the first end of the elongated shell, and a second tube fluid opening at the second end of the elongated shell;
an end plate in the first enclosed portion core between the first tube fluid opening and the core, and dividing the first enclosed portion into a first manifold portion and a first enclosed shell chamber, and a second end plate in the second end portion between the second tube fluid opening and the core, and dividing the second enclosed portion into a second manifold portion and a second enclosed shell chamber;
a first plurality of tubes extending from the first end plate, through the first enclosed shell chamber to the core, the first plurality of tubes having open ends communicating with the first manifold portion and open ends communicating with the second enclosed shell chamber;
a second plurality of tubes extending from the second end plate, through the second enclosed shell chamber to the core, the second plurality of tubes having open ends communicating with the second manifold portion and open ends communicating with the first enclosed shell chamber;
shell fluid openings at sides of the elongated shell, a first shell fluid opening communicating with the first enclosed shell chamber, and a second shell fluid opening communicating with the second enclosed shell chamber;
wherein the first enclosed shell chamber has a volume greater than the volume of the second enclosed shell chamber, and the first plurality of tubes are longer than the second plurality of tubes.

2. The shell and tube heat exchanger of claim 1 , wherein the elongated shell has a long axis, and the end plates are angled relative to the long axis.

3. The shell and tube heat exchanger of claim 2 , wherein the angle is from 15-75°.

4. The shell and tube heat exchanger of claim 2 , wherein the core is angled at the same angle as the end plates.

5. The shell and tube heat exchanger of claim 1 , wherein the tubes are polygonal with rounded corners and straight sides.

6. The shell and tube heat exchanger of claim 5 , wherein the rounded corners have a radius r and a length L, and the ratio of r/L is less than 1.45.

7. The shell and tube heat exchanger of claim 6 , wherein the ratio of r/L is from 0.05-0.55.

8. The shell and tube heat exchanger of claim 5 , wherein the polygonal tubes are triangular shaped.

9. The shell and tube heat exchanger of claim 5 , wherein the polygonal tubes are diamond-shaped.

10. The shell and tube heat exchanger of claim 5 , wherein the polygonal tubes are square shaped.

11. The shell and tube heat exchanger of claim 1 , wherein the tubes have circular cross section.

12. The shell and tube heat exchanger of claim 1 , wherein the first tube fluid opening receives high temperature fluid, the second tube fluid opening receives low temperature fluid, the first shell fluid opening exhausts low temperature fluid, and the second shell fluid opening exhausts high temperature fluid.

13. The shell and tube heat exchanger of claim 1 , wherein the first tube fluid opening exhausts low temperature fluid, the second tube fluid opening exhausts high temperature fluid, the first shell fluid opening receives high temperature fluid, and the second shell fluid opening receives low temperature fluid.

14. The shell and tube heat exchanger of claim 1 , wherein the first tube fluid opening receives low temperature fluid, the second tube fluid opening receives high temperature fluid, the first shell fluid opening exhausts high temperature fluid and the second shell fluid opening exhausts low temperature fluid.

15. The shell and tube heat exchanger of claim 1 , wherein the first tube fluid opening exhausts high temperature fluid, the second tube fluid opening exhausts low temperature fluid, the first shell fluid opening receives low temperature fluid, and the second shell fluid opening receives high temperature fluid.

16. The shell and tube heat exchanger of claim 1 , wherein the core has a length that is from 5%-75% of the length of the elongated shell.

17. The shell and tube heat exchanger of claim 1 , wherein the core has a minimum length that of 3 mm.

18. The shell and tube heat exchanger of claim 1 , wherein the minimum core length is the minimum of 3 mm or 5% of the length of the elongated shell.

19. The shell and tube heat exchanger of claim 1 , wherein the maximum core length is 75% of the length of the elongated shell.

20. A system for performing evaporation, comprising a shell and tube heat exchanger which comprises:
an elongated shell having first and second opposing ends and an open interior; a core dividing the open interior of the shell into first and second enclosed portions; a first tube fluid opening at the first end of the elongated shell, and a second tube fluid opening at the second end of the elongated shell;
an end plate in the first enclosed portion core between the first tube fluid opening and the core, and dividing the first enclosed portion into a first manifold portion and a first enclosed shell chamber, and a second end plate in the second end portion between the second tube fluid opening and the core, and dividing the second enclosed portion into a second manifold portion and a second enclosed shell chamber;
a first plurality of tubes extending from the first end plate, through the first enclosed shell chamber to the core, the first plurality of tubes having open ends communicating with the first manifold portion and open ends communicating with the second enclosed shell chamber;
a second plurality of tubes extending from the second end plate, through the second enclosed shell chamber to the core, the second plurality of tubes having open ends communicating with the second manifold portion and open ends communicating with the first enclosed shell chamber;
shell fluid openings at sides of the elongated shell, a first shell fluid opening communicating with the first enclosed shell chamber, and a second shell fluid opening communicating with the second enclosed shell chamber;
wherein the first enclosed shell chamber has a volume greater than the volume of the second enclosed shell chamber, and the first plurality of tubes are longer than the second plurality of tubes, and wherein the system is configured such that liquid enters the second plurality of tubes and is evaporated into a gas that enters the first enclosed shell chamber.

21. A system for performing condensation, comprising a shell and tube heat exchanger which comprises:
an elongated shell having first and second opposing ends and an open interior; a core dividing the open interior of the shell into first and second enclosed portions; a first tube fluid opening at the first end of the elongated shell, and a second tube fluid opening at the second end of the elongated shell;
an end plate in the first enclosed portion core between the first tube fluid opening and the core, and dividing the first enclosed portion into a first manifold portion and a first enclosed shell chamber, and a second end plate in the second end portion between the second tube fluid opening and the core, and dividing the second enclosed portion into a second manifold portion and a second enclosed shell chamber;
a first plurality of tubes extending from the first end plate, through the first enclosed shell chamber

Assignees

• Ut Battelle Llc

Inventors

• Sabau Adrian S
• Klett James W
• Polsky Yarom

Classifications

• F28F2009/228

  Oblique partitions · CPC title

• F28D7/1607

  with particular pattern of flow of the heat exchange media, e.g. change of flow direction (F28D7/1623, F28D7/1638, F28D7/1661, F28D7/1676, F28D7/1692 take precedence) · CPC title

• F28D7/10 Primary

  the conduits being arranged one within the other, e.g. concentrically {(multiple wall tubes for leak detection F28F1/003)} · CPC title

• F28D2021/0061

  for phase-change applications · CPC title

• F28F9/22

  Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates · CPC title