EP0328044B1 - Wärmetauscher - Google Patents
Wärmetauscher Download PDFInfo
- Publication number
- EP0328044B1 EP0328044B1 EP89102075A EP89102075A EP0328044B1 EP 0328044 B1 EP0328044 B1 EP 0328044B1 EP 89102075 A EP89102075 A EP 89102075A EP 89102075 A EP89102075 A EP 89102075A EP 0328044 B1 EP0328044 B1 EP 0328044B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- collecting
- heat exchanger
- tubes
- pipes
- tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 230000035882 stress Effects 0.000 description 5
- 238000005476 soldering Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000000750 progressive effect Effects 0.000 description 3
- 238000003466 welding Methods 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 230000001914 calming effect Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/06—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits having a single U-bend
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0243—Header boxes having a circular cross-section
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T29/00—Metal working
- Y10T29/49—Method of mechanical manufacture
- Y10T29/4935—Heat exchanger or boiler making
- Y10T29/49389—Header or manifold making
Definitions
- the invention relates to a heat exchanger with two collecting tubes arranged in parallel, which are connected to one another via a plurality of U-shaped sectional tubes, the collecting tubes consisting of a number of collecting tube sections which are arranged in an axially sealing manner.
- Such a heat exchanger as has become known, for example, from DE-PC-3635549 and is particularly suitable for high gas temperatures and high thermal, cyclical loads, has hitherto been produced in that the individual components, i.e. the profile tubes and header sections are firmly connected to one another by means of soldering or welding.
- the collecting tubes can consist of two half shells joined together or of individual shorter tube sections which are arranged one behind the other and are soldered together.
- GB-A-2078361 also discloses a heat exchanger with two parallel manifolds which are connected via a plurality of U-shaped tubes.
- the header pipes consist of pipe sections that are provided with plug connections and are welded together.
- a disadvantage of the designs described is that, in the event of leaks, which can occur either as a result of incorrect manufacture or as a result of material fatigue, an expensive repair or even an exchange of the entire heat exchanger is often required.
- a shock load transversely to the header tube axis unsteady inertial forces can also result in high voltage peaks at the connection points between the header tube and the profile tubes, which entails the risk of cracks and leaks, since the header tubes accommodate a large number of profile tubes.
- As a dangerous consequence of cracks there is a local weakening of the stiffness and strength of the header pipes, which triggers a progressive increase in the local stress peaks and thus a progressive damage until breakage.
- a heat exchanger is known in which a manifold consisting of several segments is also fastened Exchange plates are clamped by an inner tube that is subject to tension.
- the known heat exchanger is a version to be used stationary for hot water heating systems, which is not suitable for special loads caused by inertial forces or extreme temperature differences.
- the object of the present invention is to improve a heat exchanger of the generic type in such a way that the tightness is ensured even under mechanical shock loads or extreme temperature differences, with less high quality requirements for the connection of profile tubes / header tubes. Finally, a simplified manufacture, control, inspection and repair of the heat exchanger should be made possible.
- the object is achieved in that the manifold sections are held together by a draw tube supported on the manifold end sections and spaced concentrically within the manifolds and the draw tubes have a lower coefficient of thermal expansion than the manifolds.
- the manifolds are advantageously given increased flexural rigidity by the draw tubes, as a result of which the likelihood of cracking under impact loads is reduced.
- the header tubes are under increased axial pressure during operation of the heat exchanger, which further reduces the risk of cracks and leaks. This effect is also achieved in that the The manifolds heat up more than the internal draw tubes. By absorbing the bending load that occurs on the manifolds in the direction of the profile tube axis, their deflection and thus the stress level in the manifold walls - in particular in the fields for receiving the profile tubes - is predetermined by the draw tubes or kept at a low level.
- the draw tubes are provided with a multiplicity of openings distributed over the surface, so that the air flowing in the header tubes can enter the profile tubes unimpeded and from the profile tubes into the other header tube.
- the wall thickness is dimensioned so that the required rigidity or strength is given in every direction.
- the tensioning by means of the draw tubes is to be set so that in stationary operation sufficiently high compressive forces act on the end faces of the header sections and at the same time in the case of non-stationary ones Conditions on the draw tubes the tensile loads remain in the area of elastic expansion.
- FIG. 1 shows a heat exchanger 1, the manifolds 2 and 3 of which consist of a plurality of manifold sections 5, 6 arranged one behind the other.
- the manifolds 2 and 3 are connected to one another via a plurality of U-shaped profile tubes 21.
- the mode of operation of the heat exchanger is as follows: A cool gas flow enters the collecting tube 2 axially. The gas flow divides and flows through the large number of U-shaped profile tubes 21 embedded in the collecting tube 2 to the collecting tube 3. The gas heats up due to the hot gas flowing in the direction indicated by 36 in cross-countercurrent flow. The heated inner gas flow combines again in the collecting pipe 3 and flows axially through the collecting pipe 3.
- Fig. 2 shows a section of the heat exchanger 1 in cross section.
- the collecting pipe 2 consisting of individual collecting pipe sections 5, 6 is provided at one end with a collecting pipe end section 12 through which the internally directed gas stream is supplied.
- a closed header end portion 11 is provided at the opposite end of the header 2.
- a large number of profile tubes 21 are attached in the wall of the collecting tube 2 by means of soldering or welding. Between the individual header sections 5, 6 with the connected profile tubes 21, intermediate plates 37 are provided.
- a pull tube 15 Arranged in the interior of the collecting tube 2 is a pull tube 15 which is in a fitting connection with the collecting tube 2 at the abutment points 4 of two collecting tube sections 5, 6 lying axially one behind the other.
- the draw tube 15 is connected at points 7, 8 to the header end portions 11, 12, with a defined bracing of the draw tube 15 being set by means of screw connections, not shown.
- the draw tube 15 In the sections of the draw tube 15, which lie opposite the profile tubes 21, the draw tube 15 is provided with a number of openings 18, which can be distributed regularly over the circumference. This enables the gas flow from the inside of the draw tube 15 to the profile tubes 21 or in the header tube 3 in reverse.
- End plates 38 which are arranged parallel to the intermediate plates 27, are also fastened to the header end sections 11 and 12.
- the arrangement of the collecting pipe 2 and the drawing pipe 15 shown in FIG. 2 and described above is implemented analogously in the collecting pipe 3 and the drawing pipe 16.
- the intermediate plates 37 and end plates 38 are designed so that the header sections 5 and 6 receive narrow strips 39 without profile tubes 21 on their faces, which are necessary for reasons of strength.
- the intermediate plates 37 arranged between the manifold sections 5, 6 and the end plates 38 are connected to one another via the edge plates 40 on the arc sides 41 of the profile tubes, the edge plates 40 simultaneously serving to guide the gas. Furthermore, the intermediate plates 37 and end plates 38 together with the edge plates 40 prevent impacts in the axial direction of the collecting tube the deflection or deformation of the profile tubes by avoiding the deflection of the arc sides 41 in the direction of the collecting tube axis as a whole.
- a lug 42 is attached to one of the boundary plates 40, which is held in a certain position by a counterpart 44 fastened to the housing 43 surrounding the heat exchanger 1.
- the part of the heat exchanger 1 which is susceptible to deformation in the event of impacts in the collecting tube axial direction, ie the sum of all the profiled tubes 21, intermediate tube plates 38 and end plates 39, is thus retained.
- the intermediate plates 37 and end plates 38 are divided into two in the direction of the profile tube axis in order to compensate for the different thermal expansion of the upper and lower sides of the heat exchanger 1 and thus of the intermediate and end plates 37, 38 due to the temperature gradient in the inflow direction 36.
- the edge plates 40 are also made in two parts, since they are screwed to the intermediate and end plates 37, 38. The two parts of the edge plates 40 are connected by links 45 to ensure that the gap between the two parts remains the same under all thermal conditions in view of the required seal.
- the concentrically arranged draw tubes 15, 16 lie in the interior of the collecting tubes 2, 3. These have openings 18 distributed over the circumference.
- a shielding plate 19 is attached to the hot gas inlet-side collecting pipe 3, which ensures that the hot gas flow does not act directly on the collecting pipe 3 and the connections between the collecting pipe 3 and profile pipes 21 on the gas inlet side. As a result, the temperature gradients on the circumference of the collecting tube 3 are considerably reduced.
- the manifold end sections 11, 12 also serve to center the manifolds 2, 3 and are designed so that the heat exchanger 1 can expand freely in the manifold axial direction.
- the attachment of the draw tube 15 to the end sections 11 and 12 is shown enlarged.
- the draw tube 15 is screwed to the end sections 11, 12 by means of screws 23, 24, a gap 23 being provided between the draw tube 15 and the end section 11 in order to apply the tensile load to the draw tube 15.
- This gap 23 can advantageously be almost or completely eliminated by tightening the screw 22, as a result of which a defined prestressing of the draw tube 15 can be set.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3803947A DE3803947A1 (de) | 1988-02-10 | 1988-02-10 | Waermetauscher |
DE3803947 | 1988-02-10 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0328044A1 EP0328044A1 (de) | 1989-08-16 |
EP0328044B1 true EP0328044B1 (de) | 1991-08-28 |
Family
ID=6347008
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP89102075A Expired - Lifetime EP0328044B1 (de) | 1988-02-10 | 1989-02-07 | Wärmetauscher |
Country Status (7)
Country | Link |
---|---|
US (1) | US4940084A (enrdf_load_stackoverflow) |
EP (1) | EP0328044B1 (enrdf_load_stackoverflow) |
JP (1) | JP2678046B2 (enrdf_load_stackoverflow) |
BR (1) | BR8900566A (enrdf_load_stackoverflow) |
CA (1) | CA1305959C (enrdf_load_stackoverflow) |
DE (1) | DE3803947A1 (enrdf_load_stackoverflow) |
ES (1) | ES2025342B3 (enrdf_load_stackoverflow) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3911257C2 (de) * | 1989-04-07 | 1994-05-26 | Mtu Muenchen Gmbh | Wärmetauscher |
DE3914773C2 (de) * | 1989-05-05 | 1994-03-03 | Mtu Muenchen Gmbh | Wärmetauscher mit mindestens zwei Sammelrohren |
US5177865A (en) * | 1989-05-05 | 1993-01-12 | Mtu Motoren-Und Turbinen-Union | Method for making heat exchanger having at least two collecting pipes |
DE4118777C2 (de) * | 1991-06-07 | 2002-04-18 | Mtu Aero Engines Gmbh | Gasturbinentriebwerk mit Wärmetauscher |
US5623987A (en) * | 1992-08-04 | 1997-04-29 | Ergenics, Inc. | Modular manifold gas delivery system |
DE10236380A1 (de) * | 2002-08-08 | 2004-03-04 | Mtu Aero Engines Gmbh | Rekuperativ-Abgaswärmetauscher für ein Gasturbinentriebwerk |
US6786202B2 (en) * | 2002-09-24 | 2004-09-07 | Caterpillar Inc | Hydraulic pump circuit |
DE102006021436A1 (de) * | 2006-05-09 | 2007-11-15 | Mtu Aero Engines Gmbh | Gasturbinentriebwerk |
JP5651991B2 (ja) | 2010-05-10 | 2015-01-14 | 富士通株式会社 | ラジエータ及びそれを備えた電子機器 |
US11092384B2 (en) * | 2016-01-14 | 2021-08-17 | Hamilton Sundstrand Corporation | Thermal stress relief for heat sinks |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE214188C (enrdf_load_stackoverflow) * | ||||
US916640A (en) * | 1908-03-23 | 1909-03-30 | Robert Warg | Steam-radiator. |
GB134277A (en) * | 1918-10-24 | 1919-10-24 | John Melville James | Improvements in or relating to Radiators for Cooling Fluids. |
GB277656A (en) * | 1926-09-17 | 1928-05-10 | Jules Basin | Improvements in radiators for heating buildings |
FR669324A (fr) * | 1929-02-07 | 1929-11-14 | Radiateur de chauffage en tôle | |
DE730039C (de) * | 1935-12-11 | 1943-01-06 | Getefo Ges Fuer Tech Fortschri | Kuehler fuer Luft- und Kraftfahrzeuge |
FR859510A (fr) * | 1939-05-22 | 1940-12-20 | Chausson Usines Sa | Radiateur perfectionné |
DE1928146A1 (de) * | 1968-06-06 | 1969-12-11 | Delaney Gallay Ltd | Waermeaustauscher |
US3605882A (en) * | 1968-07-02 | 1971-09-20 | Ass Eng Ltd | Heat exchangers |
US3689972A (en) * | 1970-11-19 | 1972-09-12 | Modine Mfg Co | Method of fabricating a heat exchanger |
GB2078361A (en) * | 1980-06-24 | 1982-01-06 | Delanair Ltd | Heat exchangers and heat exchanger headers |
DE3543893A1 (de) * | 1985-12-12 | 1987-06-25 | Mtu Muenchen Gmbh | Waermetauscher |
DE3635549C1 (de) * | 1986-10-20 | 1988-03-03 | Mtu Muenchen Gmbh | Waermetauscher |
-
1988
- 1988-02-10 DE DE3803947A patent/DE3803947A1/de active Granted
-
1989
- 1989-01-30 US US07/303,921 patent/US4940084A/en not_active Expired - Fee Related
- 1989-02-07 EP EP89102075A patent/EP0328044B1/de not_active Expired - Lifetime
- 1989-02-07 ES ES89102075T patent/ES2025342B3/es not_active Expired - Lifetime
- 1989-02-08 CA CA000590428A patent/CA1305959C/en not_active Expired - Lifetime
- 1989-02-09 BR BR898900566A patent/BR8900566A/pt not_active IP Right Cessation
- 1989-02-10 JP JP1030096A patent/JP2678046B2/ja not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH01318891A (ja) | 1989-12-25 |
DE3803947C2 (enrdf_load_stackoverflow) | 1990-03-01 |
DE3803947A1 (de) | 1989-08-24 |
CA1305959C (en) | 1992-08-04 |
JP2678046B2 (ja) | 1997-11-17 |
ES2025342B3 (es) | 1992-03-16 |
US4940084A (en) | 1990-07-10 |
EP0328044A1 (de) | 1989-08-16 |
BR8900566A (pt) | 1989-10-10 |
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