WO2002090860A1 - Echangeur de chaleur pour gaz - Google Patents
Echangeur de chaleur pour gaz Download PDFInfo
- Publication number
- WO2002090860A1 WO2002090860A1 PCT/EP2002/002304 EP0202304W WO02090860A1 WO 2002090860 A1 WO2002090860 A1 WO 2002090860A1 EP 0202304 W EP0202304 W EP 0202304W WO 02090860 A1 WO02090860 A1 WO 02090860A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- heat exchanger
- gases
- exchanger
- grid
- diffuser
- Prior art date
Links
- 239000007789 gas Substances 0.000 claims abstract description 30
- 239000012530 fluid Substances 0.000 description 4
- 239000003507 refrigerant Substances 0.000 description 4
- 238000009826 distribution Methods 0.000 description 3
- 229910000679 solder Inorganic materials 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000009828 non-uniform distribution Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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
- F28D7/16—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 being arranged in parallel spaced relation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M26/00—Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
- F02M26/13—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
- F02M26/22—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with coolers in the recirculation passage
- F02M26/29—Constructional details of the coolers, e.g. pipes, plates, ribs, insulation or materials
- F02M26/32—Liquid-cooled heat exchangers
-
- 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
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/0278—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of stacked distribution plates or perforated plates arranged over end plates
-
- 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
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
- F28D21/0003—Recuperative heat exchangers the heat being recuperated from exhaust gases
Definitions
- the present invention relates to a heat exchanger for gases, of the type comprising a plurality of conduits mounted in parallel in which circulate the gases to be cooled as well as an inlet manifold interposed between the inlet gas manifold. and the entrance to these conduits.
- the gases circulate via a series of parallel tubes or conduits, which during this circulation are cooled by heat exchange with a refrigerant which circulates outside the conduits through which the gases pass.
- these exchangers can be in the form of a bundle of tubes arranged inside a box in which the refrigerant is circulated, or they can be produced by a series of parallel plates which constitute the heat exchange surfaces, so that the exhaust gases and the refrigerant circulate alternately in the conduits formed between two plates.
- the gases supplying the tube bundle or the exchanger conduits arrive via an inlet pipe; since the diameter of the inlet pipe is smaller than the diameter of the housing and of the tube bundle of the exchanger, between the two is interposed an inlet manifold which widens by gradually.
- the distance between the gas inlet pipe and the tube bundle is generally reduced in order to prevent the exchanger from occupying too large a space; this has the consequence that the distribution of the gases is not made uniformly between all the tubes of the exchanger bundle and that a significant proportion of these gases pass through the tubes situated in the center of the bundle and only a small part of the gas passes through the outermost tubes.
- the object of the present invention is to provide a solution to the drawbacks mentioned above, by proposing a heat exchanger having the same dimensions as those of a conventional exchanger but offering improved power and thermal efficiency with at the same time a reduced cost.
- the heat exchanger according to the invention is characterized in that in the inlet manifold is placed, for example fixed, a diffuser element.
- the diffuser element may be perforated.
- the diffuser element is substantially flat.
- the diffuser element is arranged substantially perpendicular to the direction of circulation of the gases to be cooled.
- the distribution of gas in the ducts of the exchanger becomes uniform, thus resulting in better efficiency of the device; at the same time, in practice, the integration of this element in the conventional type exchanger is very simple due to its configuration, and it does not cause a significant increase in its cost.
- this exchanger is particularly suitable for cooling the exhaust gases of vehicles which are equipped with exhaust gas recirculation systems towards the intake (EGR, "Exhaust Gas Recycling”).
- such a diffuser comprises a plate provided with a plurality orifices.
- the plate orifices can be either circular or polygon-shaped, and their size can vary from 1 to 20 mm.
- this diffuser comprises a grid; preferably, this grid will be produced from a wire of 0.2 to 3 mm and a grid pitch of between 1 and 10 mm.
- Figure 1 schematically shows the inlet side of a heat exchanger of a bundle of tubes according to the invention.
- FIGS 2 and 3 show two other embodiments of the exchanger diffuser.
- the exchanger of Figure 1 consists of a housing 1 comprising a bundle of parallel tubes 2, intended for the passage of the gases to be cooled. Inside the housing 1, outside the tubes 2, a refrigerant circulates from the inlet 3 to an outlet (not shown).
- the gases to be cooled enter the exchanger through an inlet pipe 4 and via an inlet manifold 5, which gradually widens.
- the housing 1 is cylindrical and the inlet manifold 5 therefore has a frustoconical shape.
- a flat and perforated diffuser element is placed in the exchanger, which consists in Figures 1 and 2 in a plate 6 provided with a plurality of circular orifices 7 evenly distributed.
- the gas flow which circulates via the inlet pipe 4 is deflected by the plate 6, this having the effect of distributing it in all directions so that a greater proportion of fluid reaches the tubes located most at the periphery of the beam .
- the perforated plate 6 can be placed at any point of the inlet manifold 5, that is to say, more or less close to the inlet of the tubes 2; there can be between 1 and 200 orifices 7 on the plate 6, everything depends on the size of the exchanger, and each of them can have a diameter between 1 and 20 mm, preferably between 6 and 8 mm.
- the orifices 7 can be distributed in different ways on the plate 6, and can have the shape of a polygon rather than that of a circle. It is also possible to associate orifices of different shapes on the same plate, for example to provide a larger passage section in certain areas rather than in others.
- the thickness of the plate can vary between 0.5 mm and 3 mm approximately.
- the diffuser 6 could consist of a grid 6 ', as shown in Figure 3, in place of the perforated plate.
- the grid 6 ′ can be made of steel wire 8 whose diameter is between 0.2 mm and 6 mm and have a grid pitch between 1 and 10 mm; the step of grid is defined as the distance from one wire to another, that is to say the dimension of each hole in the grid.
- the grid 6 has the same function as the plate 6: it distributes the gas flow so that it reaches all the tubes of the bundle in the same proportion.
- the diffuser whether it is a perforated plate 6 or a grid 6 ′, is fixed to the inlet manifold 5, preferably by a few solder points, although it is possible to stick with a suitable adhesive or weld it with a supply of solder material. In some cases, it may be possible to manufacture the inlet manifold 5 directly with the diffuser 6,6 ', for example by molding.
- the test was carried out with an exchanger with a shell diameter of 54 mm (case diameter), with a stainless steel diffuser 45 mm in diameter and 1 mm thick, placed 8 mm from the inlet. of the tube bundle.
- the results of the test are shown in the following table.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0320641A GB2391931A (en) | 2001-03-01 | 2002-02-26 | Heat exchanger for gas |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ES0100484 | 2001-03-01 | ||
ES200100484A ES2198179B1 (es) | 2001-03-01 | 2001-03-01 | Intercambiador de calor para gases. |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2002090860A1 true WO2002090860A1 (fr) | 2002-11-14 |
Family
ID=8496933
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2002/002304 WO2002090860A1 (fr) | 2001-03-01 | 2002-02-26 | Echangeur de chaleur pour gaz |
Country Status (3)
Country | Link |
---|---|
ES (1) | ES2198179B1 (fr) |
GB (1) | GB2391931A (fr) |
WO (1) | WO2002090860A1 (fr) |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006100069A1 (fr) * | 2005-03-24 | 2006-09-28 | Behr Gmbh & Co. Kg | Echangeur thermique pour gaz d'echappement, notamment refroidisseur de gaz d'echappement pour le recyclage des gaz d'echappement dans les vehicules a moteur |
WO2010125037A1 (fr) * | 2009-04-29 | 2010-11-04 | Basf Se | Échangeur de chaleur à faisceau tubulaire et procédé destiné à l'évacuation de substances volatiles hors d'une solution polymère |
EP2273095A1 (fr) * | 2009-07-10 | 2011-01-12 | Behr GmbH & Co. KG | Echangeur thermique, système de recyclage des gaz d'échappement et moteur à combustion interne |
WO2012007344A3 (fr) * | 2010-07-16 | 2012-03-29 | Alfa Laval Corporate Ab | Dispositif d'échange de chaleur comportant un système perfectionné pour distribuer du fluide réfrigérant |
CN102650834A (zh) * | 2011-02-28 | 2012-08-29 | Asml荷兰有限公司 | 气体歧管、光刻设备用模块、光刻设备及器件制造方法 |
WO2012104438A3 (fr) * | 2011-02-04 | 2013-03-28 | Behr Gmbh & Co. Kg | Échangeur de chaleur |
FR3016027A1 (fr) * | 2014-01-02 | 2015-07-03 | Electricite De France | Echangeur thermique comprenant une grille |
JP2017032232A (ja) * | 2015-08-04 | 2017-02-09 | パナソニック株式会社 | 蒸発器及びランキンサイクルシステム |
EP2889570B1 (fr) | 2012-07-09 | 2017-08-09 | Sumitomo Precision Products Co., Ltd. | Échangeur thermique |
US10677503B2 (en) * | 2008-01-02 | 2020-06-09 | Johnson Controls Technology Company | Heat exchanger |
EP3702716A4 (fr) * | 2017-11-17 | 2020-12-16 | LG Chem, Ltd. | Échangeur de chaleur |
CN112432543A (zh) * | 2020-11-20 | 2021-03-02 | 无锡锡州机械有限公司 | 一种烟气分配器 |
WO2021171223A1 (fr) * | 2020-02-26 | 2021-09-02 | Sabic Global Technologies B.V. | Dispositif à impact pour protection de tube d'entrée d'échangeur de chaleur |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL2018753B1 (en) * | 2017-04-20 | 2018-05-08 | Apex Int Holding B V | Gas Flow Conditioner Device for a Heat Exchanger |
DE112018007657B4 (de) * | 2018-05-24 | 2022-10-27 | Mitsubishi Electric Corporation | Rohrbündel-wärmetauscher |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2768814A (en) * | 1950-10-27 | 1956-10-30 | Frey | Plate warmer exchanger |
US3795259A (en) * | 1971-07-07 | 1974-03-05 | Stal Refrigeration Ab | Device for evenly mixing and distributing a gas and liquid mixture |
EP0043383A1 (fr) * | 1980-07-08 | 1982-01-13 | Riedel Kälte- und Klimatechnik GmbH & Co, KG | Evaporateur pour liquides et/ou gaz, spécialement pour équipements frigorifiques et thermopompes |
DE3612841A1 (de) * | 1986-04-16 | 1987-10-22 | Steinmueller Gmbh L & C | Waermetauscher fuer den waermetausch zwischen einem heissen gas und einem in rohrbuendelheizflaechen gefuehrten stroemungsmittel, insbesondere waermetauscher fuer gasgekuehlte hochtemperaturreaktoren |
DE3908277A1 (de) * | 1989-03-14 | 1990-09-20 | Dmp Mineraloel Petrochemie Gmb | Erosionsschutz fuer waermetauscher |
JPH0735492A (ja) * | 1993-07-26 | 1995-02-07 | Nissan Motor Co Ltd | ガスタービンの流路構造 |
US5415223A (en) * | 1993-08-02 | 1995-05-16 | Calsonic International, Inc. | Evaporator with an interchangeable baffling system |
JPH07159076A (ja) * | 1993-12-08 | 1995-06-20 | Nissan Motor Co Ltd | 積層型熱交換器 |
EP1079194A2 (fr) * | 1999-08-23 | 2001-02-28 | Nippon Shokubai Co., Ltd. | Méthode pour empêcher le blocage d'un échangeur de chaleur à plaques |
-
2001
- 2001-03-01 ES ES200100484A patent/ES2198179B1/es not_active Expired - Fee Related
-
2002
- 2002-02-26 GB GB0320641A patent/GB2391931A/en not_active Withdrawn
- 2002-02-26 WO PCT/EP2002/002304 patent/WO2002090860A1/fr unknown
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2768814A (en) * | 1950-10-27 | 1956-10-30 | Frey | Plate warmer exchanger |
US3795259A (en) * | 1971-07-07 | 1974-03-05 | Stal Refrigeration Ab | Device for evenly mixing and distributing a gas and liquid mixture |
EP0043383A1 (fr) * | 1980-07-08 | 1982-01-13 | Riedel Kälte- und Klimatechnik GmbH & Co, KG | Evaporateur pour liquides et/ou gaz, spécialement pour équipements frigorifiques et thermopompes |
DE3612841A1 (de) * | 1986-04-16 | 1987-10-22 | Steinmueller Gmbh L & C | Waermetauscher fuer den waermetausch zwischen einem heissen gas und einem in rohrbuendelheizflaechen gefuehrten stroemungsmittel, insbesondere waermetauscher fuer gasgekuehlte hochtemperaturreaktoren |
DE3908277A1 (de) * | 1989-03-14 | 1990-09-20 | Dmp Mineraloel Petrochemie Gmb | Erosionsschutz fuer waermetauscher |
JPH0735492A (ja) * | 1993-07-26 | 1995-02-07 | Nissan Motor Co Ltd | ガスタービンの流路構造 |
US5415223A (en) * | 1993-08-02 | 1995-05-16 | Calsonic International, Inc. | Evaporator with an interchangeable baffling system |
JPH07159076A (ja) * | 1993-12-08 | 1995-06-20 | Nissan Motor Co Ltd | 積層型熱交換器 |
EP1079194A2 (fr) * | 1999-08-23 | 2001-02-28 | Nippon Shokubai Co., Ltd. | Méthode pour empêcher le blocage d'un échangeur de chaleur à plaques |
Non-Patent Citations (2)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 1995, no. 05 30 June 1995 (1995-06-30) * |
PATENT ABSTRACTS OF JAPAN vol. 1995, no. 09 31 October 1995 (1995-10-31) * |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2110636A1 (fr) * | 2005-03-24 | 2009-10-21 | Behr GmbH & Co. KG | Echangeur thermique pour gaz d'échappement, notamment refroidisseur de gaz d'échappement pour le recyclage des gaz d'échappement dans les véhicules à moteur |
WO2006100069A1 (fr) * | 2005-03-24 | 2006-09-28 | Behr Gmbh & Co. Kg | Echangeur thermique pour gaz d'echappement, notamment refroidisseur de gaz d'echappement pour le recyclage des gaz d'echappement dans les vehicules a moteur |
US10677503B2 (en) * | 2008-01-02 | 2020-06-09 | Johnson Controls Technology Company | Heat exchanger |
WO2010125037A1 (fr) * | 2009-04-29 | 2010-11-04 | Basf Se | Échangeur de chaleur à faisceau tubulaire et procédé destiné à l'évacuation de substances volatiles hors d'une solution polymère |
CN102422111A (zh) * | 2009-04-29 | 2012-04-18 | 巴斯夫欧洲公司 | 用于从聚合物溶液中除去挥发性物质的壳管式热交换器和方法 |
US8657921B2 (en) | 2009-04-29 | 2014-02-25 | Styrolution GmbH | Shell and tube heat exchanger and method for removing volatile substances from a polymer solution |
EP2273095A1 (fr) * | 2009-07-10 | 2011-01-12 | Behr GmbH & Co. KG | Echangeur thermique, système de recyclage des gaz d'échappement et moteur à combustion interne |
EP2667007A1 (fr) * | 2009-07-10 | 2013-11-27 | Behr GmbH & Co. KG | Echangeur thermique, système de recyclage des gaz d'échappement et moteur à combustion interne |
US9310143B2 (en) | 2010-07-16 | 2016-04-12 | Alfa Laval Corporate Ab | Heat exchange device with improved system for distributing coolant fluid |
WO2012007344A3 (fr) * | 2010-07-16 | 2012-03-29 | Alfa Laval Corporate Ab | Dispositif d'échange de chaleur comportant un système perfectionné pour distribuer du fluide réfrigérant |
EP2671032B1 (fr) | 2011-02-04 | 2018-05-09 | MAHLE Behr GmbH & Co. KG | Échangeur de chaleur |
US9599409B2 (en) | 2011-02-04 | 2017-03-21 | Mahle International Gmbh | Heat exchanger for vehicle with two block design |
WO2012104438A3 (fr) * | 2011-02-04 | 2013-03-28 | Behr Gmbh & Co. Kg | Échangeur de chaleur |
CN102650834A (zh) * | 2011-02-28 | 2012-08-29 | Asml荷兰有限公司 | 气体歧管、光刻设备用模块、光刻设备及器件制造方法 |
EP2889570B1 (fr) | 2012-07-09 | 2017-08-09 | Sumitomo Precision Products Co., Ltd. | Échangeur thermique |
FR3016027A1 (fr) * | 2014-01-02 | 2015-07-03 | Electricite De France | Echangeur thermique comprenant une grille |
JP2017032232A (ja) * | 2015-08-04 | 2017-02-09 | パナソニック株式会社 | 蒸発器及びランキンサイクルシステム |
EP3702716A4 (fr) * | 2017-11-17 | 2020-12-16 | LG Chem, Ltd. | Échangeur de chaleur |
US11209213B2 (en) | 2017-11-17 | 2021-12-28 | Lg Chem, Ltd. | Heat exchanger |
WO2021171223A1 (fr) * | 2020-02-26 | 2021-09-02 | Sabic Global Technologies B.V. | Dispositif à impact pour protection de tube d'entrée d'échangeur de chaleur |
CN112432543A (zh) * | 2020-11-20 | 2021-03-02 | 无锡锡州机械有限公司 | 一种烟气分配器 |
Also Published As
Publication number | Publication date |
---|---|
ES2198179A1 (es) | 2004-01-16 |
GB2391931A (en) | 2004-02-18 |
GB0320641D0 (en) | 2003-10-01 |
ES2198179B1 (es) | 2004-11-16 |
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