Helically coiled heat exchanger

Patent metadata

Field	Value
Publication number	US-10823508-B2
Application number	US-201716093182-A
Country	US
Kind code	B2
Filing date	Apr 12, 2017
Priority date	Apr 14, 2016
Publication date	Nov 3, 2020
Grant date	Nov 3, 2020

Abstract

A heat exchanger for indirect heat exchange between a first and a second medium is provided with a shell space for receiving the first medium, and a tube bundle arranged in the shell space and for receiving the second medium. The tubes are helically wound in a number of tube layers onto a core tube. The tube bundle includes a first tube layer which is positioned further outward in the radial direction of the tube bundle from an adjacent second tube layer. The heat exchanger includes at least one spacer and the first tube bundle is supported against the second tube bundle via the at least one spacer. The at least one spacer has a flow-directing region designed to deflect part of the first medium flowing along a tube of the first tube layer in the direction of the second tube layer situated further inwards in the radical direction.

First claim

The invention claimed is:

1. A heat exchanger for indirect exchange of heat between a first and a second medium, the heat exchanger comprising:
a shell space for accommodating the first medium,
a tube bundle arranged in the shell space having a plurality of tubes for accommodating the second medium, wherein each tube is helically coiled onto a core tube and the tube bundle has multiple tube layers arranged one on top of the other, wherein the tube bundle has a radial direction that extends outward from the core tube, and
at least one spacer,
wherein said tube bundle has a first tube layer which is positioned further outward in the radial direction of the tube bundle from an adjacent second tube layer, and said first tube layer is supported against said second tube layer via said at least one spacer, and
wherein the at least one spacer has a flow-guiding means which is configured to divert a part of the first medium, which part flows along the first tube layer in the shell space towards the second tube layer which is positioned further inward in the radial direction of the tube bundle from the adjacent first tube layer.

2. The heat exchanger as claimed in claim 1 , wherein said flow-guiding means has an end side of the spacer which connects a front side, facing away from the core tube, of the spacer to a rear side, facing the core tube, of the spacer.

3. The heat exchanger as claimed in claim 2 , wherein said end side has an inclination toward the second tube layer such that the part of the first medium flows along the tube of the first tube layer and against the end side and is diverted by the end side towards the second tube layer.

4. The heat exchanger as claimed in claim 1 , wherein said flow-guiding means has at least one guiding element which is fixed to a base of the spacer, wherein said base extends along a longitudinal axis and the first tube layer is supported against the second tube layer via said base.

5. The heat exchanger as claimed in claim 4 , wherein the at least one guiding element forms an impact surface which has an inclination towards the second tube layer such that the part of the first medium flows along a tube of the first tube layer and against the impact surface and is diverted by the impact surface towards the second tube layer.

6. The heat exchanger as claimed in claim 4 , wherein the at least one guiding element extends sectionally between adjacent tube sections of the second tube layer.

7. The heat exchanger as claimed in claim 4 , wherein the at least one guiding element is, in relation to the flow direction of said part of the first medium, arranged on an edge section of the spacer which is positioned upstream.

8. The heat exchanger as claimed in claim 4 , wherein the at least one guiding element is, in relation to the flow direction of said part of the first medium, arranged on an edge section of the spacer which is positioned downstream.

9. The heat exchanger as claimed in claim 1 , wherein the core tube extends along a longitudinal axis.

10. The heat exchanger as claimed in claim 9 , wherein the heat exchanger has a shell which surrounds the shell space and which extends coaxially with the core tube along the longitudinal axis.

11. The heat exchanger as claimed in claim 9 , wherein the at least one spacer and/or said flow-guiding means extends along the longitudinal axis.

12. The heat exchanger as claimed in claim 1 , wherein said flow-guiding means is configured to divert the part of the first medium, which flows along the first tube layer from the top downward towards the second tube layer.

13. The heat exchanger as claimed in claim 1 , wherein the flow-guiding means has a plurality of channels which are provided in the at least one spacer and which are configured to divert the part of the first medium, which flows along the first tube layer from the top downward towards the second tube layer.

14. The heat exchanger as claimed in claim 1 , wherein the heat exchanger has a plurality of said spacer elements between the first and the second tube layer, wherein the spacer elements each have a flow-guiding means which is configured to divert a part of the first medium flowing along the first tube layer towards the second tube layer.

15. The heat exchanger as claimed in claim 1 , wherein the heat exchanger has spacer elements between multiple or between all adjacent tube layers of the heat exchanger wherein each spacer element has a flow-guiding means configured to divert a part of the first medium, which part flows along a tube layer towards an adjacent tube layers which is positioned further inward in the radial direction of the tube bundle.

16. The heat exchanger as claimed in claim 15 , wherein the number of spacers arranged between adjacent tube layers is constant, wherein spacers are arranged one on top of the other in the radial direction of the tube bundle to support the tube layers.

17. The heat exchanger as claimed in claim 1 , wherein
(a) said flow-guiding means has an end side of the spacer which connects a front side, facing away from the core tube, of the spacer to a rear side, facing the core tube, of the spacer, and wherein said end side has an inclination toward the second tube layer such that the part of the first medium flows along the tube of the first tube layer and against the end side and is diverted by the end side towards the second tube layer; or
(b) said flow-guiding means has at least one guiding element which is fixed to a base of the spacer, wherein said base extends along a longitudinal axis and the first tube layer is supported against the second tube layer via said base, and the at least one guiding element forms an impact surface which has an inclination towards the second tube layer such that the part of the first medium flows along a tube of the first tube layer and against the impact surface and is diverted by the impact surface towards the second tube layer.

Assignees

• Linde Ag

Inventors

• Steinbauer Manfred
• Kerber Christiane
• Spreemann Jurgen
• Braun Konrad
• Acher Thomas

Classifications

• F28F13/06

  by affecting the pattern of flow of the heat-exchange media {(F28F13/003 takes precedence; static flow control means in header boxes F28F9/026)} · CPC title

• F28F9/0132

  formed by slats, tie-rods, articulated or expandable rods · CPC title

• F28D7/022

  the conduits of two or more media in heat-exchange relationship being helically coiled, the coils having a cylindrical configuration · CPC title

• F28D7/024 Primary

  the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration · CPC title

• F28F9/22

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