HEAT EXCHANGER FOR THE THERMAL COUPLING OF TWO FLUIDS
20230124890 ยท 2023-04-20
Inventors
- Dennis Aul (Stuttgart, DE)
- Uwe FOERSTER (Erdmannhausen, DE)
- Martin Sievers (Kernen Im Remstel, DE)
- Dawid Trawinski (Ostrow Weilkopolski, PL)
Cpc classification
F28D7/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F9/028
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28D1/05366
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
Abstract
A heat exchanger for the thermal coupling of two fluids may include an inflow pipe defining a pipe longitudinal centre axis. A fluid inlet may be arranged on the inflow pipe. A plurality of flat tubes leading into the inflow pipe may be arranged on the inflow pipe adjacent to the fluid inlet. The first fluid stream may be flowable along a first fluid path extending from the fluid inlet through the inflow pipe and the plurality of flat tubes. The flat tubes may extend through a second fluid path for a second fluid stream of fluid and may be flowed about by the second fluid stream during operation. The heat exchanger may further include passage screen aperture interacting with the heat exchanger fluid and through which the first fluid stream is flowable. The passage screen aperture may be fluidically connected in series with the flat tubes.
Claims
1. A heat exchanger for the thermal coupling of two fluids, comprising: an inflow pipe defining a pipe longitudinal centre axis; a fluid inlet arranged on the inflow pipe via which a first fluid stream of heat exchanger fluid is flowable into the inflow pipe; a plurality of flat tubes arranged on the inflow pipe adjacent to the fluid inlet in a direction of the pipe longitudinal centre axis, the plurality of flat pipes disposed spaced apart from one another along the pipe longitudinal centre axis and each leading into the inflow pipe such that the first fluid stream is flowable along a first fluid path extending from the fluid inlet through the inflow pipe and the plurality of flat tubes; the plurality of flat tubes extending through a second fluid path for a second fluid stream of fluid such that the plurality of flat tubes are flowed through by the first fluid stream and flowed about by the second fluid stream during operation; a passage screen aperture interacting with the heat exchanger fluid and through which the first fluid stream which is flowable; and wherein the passage screen aperture is fluidically connected in series with the plurality of flat tubes.
2. The heat exchanger according to claim 1, wherein the passage screen aperture is arranged upstream of the plurality of flat tubes with respect to the first fluid stream.
3. The heat exchanger according to claim 1, wherein the passage screen aperture is connected downstream off the fluid inlet with respect to the first fluid stream.
4. The heat exchanger according to claim 1, further comprising a passage screen in which the passage screen aperture is arranged, wherein the passage screen is arranged in the first fluid path between the fluid inlet and the plurality of flat tubes.
5. The heat exchanger according to claim 4, wherein a gap between the passage screen aperture of the passage screen and a first flat tube of the plurality of flat tubes, which with respect to the fluid inlet is disposed next in the direction of the pipe longitudinal centre axis and directly adjacent to the passage screen, has a length measured parallel to the pipe longitudinal centre axis of 2.0 mm to 9.0 mm.
6. The heat exchanger according to claim 1, further comprising a passage screen on which the passage screen aperture is arranged, wherein the passage screen has a surrounding outer edge via which the passage screen supports itself, at least in portions touchingly, on at least one pipe inner circumferential surface of the inflow pipe.
7. The heat exchanger according to claim 6, wherein: the outer edge at least one of includes and forms a stiffening reinforcing the passage screen against a shape change; and the outer edge has a thickness of 1.4 mm to 3.0 mm.
8. The heat exchanger according to claim 1, further comprising a passage screen in which the passage screen aperture is arranged, wherein: the passage screen includes at least one insert tab projecting, with respect to a screen centre of the passage screen radially to an outside; the at least one insert tab is inserted into a tab groove of the inflow pipe at least one of positively and non-positively coupling the passage screen to the inflow pipe; and the tab groove is formed complementarily to the at least one insert tab.
9. The heat exchanger according to claim 6, wherein: the inflow pipe is divided along the pipe longitudinal centre axis into a longitudinal lower shell and a longitudinal upper shell; and the outer edge of the passage screen is split into a first circumferential receiving portion for receiving the longitudinal lower shell and a second circumferential receiving portion, which is recessed with respect to the first receiving portion, for receiving the longitudinal upper shell.
10. The heat exchanger according to claim 1, further comprising a passage screen in which the passage screen aperture is arranged, wherein the passage screen at least one of includes and forms at least one flow separation edge framing the passage screen aperture at least in portions.
11. The heat exchanger according to claim 1, wherein the passage screen aperture defines a circular segment-shaped opening contour.
12. The heat exchanger according to claim 1, further comprising a passage screen in which the passage screen aperture is arranged, wherein: the passage screen defines a screen centre; a plane extends through the screen centre; the plane extends parallel to the pipe longitudinal centre axis and is aligned orthogonally with respect to a plurality of flat tube centre axes defined by the plurality of flat tubes such that the plane divides the passage screen into a first side facing away from the plurality of flat tubes and a second side facing the plurality of flat tubes; and the passage screen aperture is arranged on the first side of the passage screen.
13. The heat exchanger according to claim 1, further comprising a passage screen on which the passage screen aperture is arranged, wherein: the passage screen defines a surface area; and a passage area of the passage screen aperture amounts to 5% or more of the surface area.
14. The heat exchanger according to claim 1, further comprising a passage screen on which the passage screen aperture is arranged, wherein: the passage screen defines a surface area; and a passage area of the passage screen aperture amounts to 5% to 50% of the surface area.
15. The heat exchanger according to claim 1, further comprising a passage screen in which the passage screen aperture is arranged, wherein: the passage screen includes at least one flow separation edge framing the passage screen aperture; and the at least one flow separation edge interacts fluidically with the first fluid stream flowing through the passage screen aperture such that, downstream of the passage screen, a liquid phase of the heat exchanger fluid in the first fluid stream is distributed in a gas phase of the heat exchanger fluid and evenly distributed over the plurality of fluid tubes.
16. The heat exchanger according to claim 1, wherein: the inflow pipe is defined by a longitudinal upper shell and a longitudinal lower shell that are connected to one another; the passage screen has a surrounding outer edge including: a first contour portion engaging an inner surface of the lower shell; a second contour portion engaging an inner surface of the upper shell; and two step portions connecting the first contour portion and the second contour portion; and two opposing ends of the upper shell project into the lower shell, contact the inner surface of the lower shell, and abut a respective step portion of the two step portions of the outer edge of the passage screen.
17. The heat exchanger according to claim 16, wherein: the passage screen further includes a first insert tab and a second insert tab projecting outward from the second contour portion of the outer edge; the first insert tab is received in a first tab groove of the upper shell and the second insert tab is received in a second tab groove of the upper shell; and the first insert tab and the second insert tab extend parallel to one another.
18. The heat exchanger according to claim 1, wherein: the inflow pipe is defined by a longitudinal upper shell and a longitudinal lower shell that are connected to one another; the passage screen has, in a cross-section perpendicular to the first fluid stream, an upper half disposed adjacent to the upper shell and a lower half disposed adjacent to the lower shell; and the passage screen aperture is disposed entirely within the upper half of the passage screen.
19. A heat exchanger for the thermal coupling of two fluids, comprising: an inflow pipe having a pipe longitudinal centre axis; the inflow pipe including a fluid inlet via which a heat exchanger fluid is flowable into the inflow pipe; a plurality of flat tubes arranged on the inflow pipe spaced apart from one another in a direction of the pipe longitudinal centre axis, the plurality of flat tubes each in fluid communication with the inflow pipe such that a first fluid stream of the heat exchanger fluid is flowable along a first fluid path extending from the fluid inlet, through the inflow pipe into the plurality of flat tubes, and through the plurality of flat tubes; the plurality of flat tubes extending through a second fluid path of a fluid such that a second fluid stream of the fluid is flowable around an exterior of the plurality of flat tubes; a passage screen arranged within the inflow pipe between the fluid inlet and the plurality of flat tubes relative to a flow direction of the first fluid flow; and wherein the passage screen includes a passage screen aperture interacting with the heat exchanger fluid and through which the first fluid stream is flowable.
20. A heat exchanger for the thermal coupling of two fluids, comprising: an inflow pipe having a pipe longitudinal centre axis; the inflow pipe including a fluid inlet via which a heat exchanger fluid is flowable into the inflow pipe; a plurality of flat tubes arranged on the inflow pipe spaced apart from one another in a direction of the pipe longitudinal centre axis, the plurality of flat tubes each in fluid communication with the inflow pipe such that a first fluid stream of the heat exchanger fluid is flowable along a first fluid path extending from the fluid inlet, through the inflow pipe into the plurality of flat tubes, and through the plurality of flat tubes; the plurality of flat tubes extending through a second fluid path of a fluid such that a second fluid stream of the fluid is flowable around an exterior of the plurality of flat tubes; a passage screen arranged within the inflow pipe between the fluid inlet and a flat tube of the plurality of flat tubes disposed closest to the fluid inlet; the passage screen disposed downstream of the fluid inlet and upstream of the plurality of flat tubes relative to the first fluid flow; wherein the passage screen includes a circular segment-shaped passage screen aperture through which the first fluid stream is flowable; and wherein the passage screen and the passage screen aperture are structured and arranged to interact with the first fluid stream such that swirl flows in the heat exchanger fluid are reduced.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0025] It shows, in each case schematically
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DETAILED DESCRIPTION
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[0033] Away from the inflow pipe 3 and from the outflow pipe 34, the said flat tubes 6, 12 extend through a second fluid path 9 for a second fluid stream 32 of cooling fluid, so that the flat tubes 6, 12 can be flowed through by the first fluid stream 5 and flowed about by the second fluid stream 32. This means that the two fluid streams 5, 32 intersect. By way of this, a heat energy stream can be exchanged between the two fluid streams 5, 32. Practically, the first fluid stream 5 functions as heat source and the second fluid stream 32 as heat sink or vice versa.
[0034] With respect to
[0035] The said passage screen 11 or the passage screen aperture 10 is arranged in the first fluid path 8 between the fluid inlet 4 and a first flat tube 12 of these flat tubes 6, 12 which with respect to the fluid inlet 4 is located next in the direction of the pipe longitudinal centre axis 2 and directly adjacent. Purely exemplarily, a gap 13 to be measured parallel to the pipe longitudinal centre axis 2 is adjusted between the passage screen 11 or the passage screen aperture 10 and the first flat tube 12. This gap can lie within a range between 2.0 mm to 9.0 mm or preferably within a range between 3.0 mm and 6.0 mm.
[0036] With respect to
[0037] In
[0038] In
[0039] Both in
[0040] With respect to
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