EP1682842A1 - Canal d'ecoulement pour dispositif de transfert de chaleur et dispositif de transfert de chaleur comprenant de tels canaux d'ecoulement - Google Patents

Canal d'ecoulement pour dispositif de transfert de chaleur et dispositif de transfert de chaleur comprenant de tels canaux d'ecoulement

Info

Publication number
EP1682842A1
EP1682842A1 EP04786965A EP04786965A EP1682842A1 EP 1682842 A1 EP1682842 A1 EP 1682842A1 EP 04786965 A EP04786965 A EP 04786965A EP 04786965 A EP04786965 A EP 04786965A EP 1682842 A1 EP1682842 A1 EP 1682842A1
Authority
EP
European Patent Office
Prior art keywords
flow channel
structural elements
channel according
flow
rows
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.)
Granted
Application number
EP04786965A
Other languages
German (de)
English (en)
Other versions
EP1682842B1 (fr
Inventor
Peter Geskes
Rainer Lutz
Ulrich Maucher
Martin Schindler
Michael Schmidt
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mahle Behr GmbH and Co KG
Original Assignee
Behr GmbH and Co KG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Behr GmbH and Co KG filed Critical Behr GmbH and Co KG
Priority to EP10181882.1A priority Critical patent/EP2267393B1/fr
Publication of EP1682842A1 publication Critical patent/EP1682842A1/fr
Application granted granted Critical
Publication of EP1682842B1 publication Critical patent/EP1682842B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/02—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by influencing fluid boundary
    • 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 invention relates to a flow channel of a heat exchanger through which a medium can flow in a flow direction.
  • the invention also relates to a heat exchanger with flow channels according to the preamble of claim 40.
  • Flow channels for heat exchangers are from a first medium, for. B. flows through an exhaust gas or a liquid coolant and delimit this first medium from a second medium to which the heat of the ⁇ first medium is to be transferred.
  • Flow channels of this type can be tubes with a round cross section, rectangular tubes, flat tubes or pairs of disks in which two plates or disks are connected at the edge.
  • the media that are in heat exchange with each other are different, e.g. B. flows in the tubes a hot, soot-laden exhaust gas, and on the outside the exhaust pipes are flowed around by a liquid coolant, which results in different heat transfer conditions on the inside and the outside of the pipes.
  • a heat exchanger in particular a coolant / air cooler with flat tubes and corrugated fins, in which the flat sides of the flat tubes have a structure consisting of structural elements.
  • the structural elements are elongated, arranged in a V-shape in rows transversely to the coolant flow direction or transversely to the longitudinal axis of the tubes and act as eddies to increase the heat transfer on the coolant side.
  • the vortex generators are embossed in both opposite pipe walls and protrude inwards into the coolant flow.
  • the rows of vortex generators on one flat tube side are offset in the flow direction compared to the rows on the other flat tube side. This also makes it possible to dimension the inwardly projecting height of the vortex generators to be greater than half the inside width of the flat tube cross section.
  • EP-A 1 061 319 has disclosed a flat tube for a motor vehicle radiator, which has a structure on its flat sides which consists of individual elongate structural elements arranged in rows.
  • the structural elements which are arranged in rows in particular, are essentially opposite one another on the one and the other side of the flow channel, that is to say seen in the flow direction, are each arranged approximately at the same height.
  • the opposing structural elements or rows can also be offset from one another in the direction of flow, but only to the extent that there is still an overlap.
  • Structural elements that protrude from one and the other heat exchanger surface and protrude into the flow channel thus simultaneously intervene in the flow and cause a swirling of the flow, which results in an improvement in the heat transfer on the inside of the flow channel.
  • a soot deposits prevented.
  • the pressure loss is kept within reasonable limits.
  • the flow within the flow channel is thus disturbed from both sides at the same time, ie both boundary layers are detached at the same time, which leads to a particularly strong turbulence.
  • the opposing structural elements or rows of structural elements can also be located on the outside of the flow channel - on the coolant side in the case of an exhaust gas cooler.
  • a row with structural elements is formed by one or more structural elements which are arranged essentially next to one another in the direction of flow P.
  • a row can also be formed by a single structural element, next to which, for example, no further structural elements are arranged.
  • the structural elements can be straight or curved, ie with a constant or variable outflow angle to the flow direction.
  • the change in the outflow angle from a relatively large inflow angle to the outflow angle results in a “gentle” deflection of the flow and thus a somewhat reduced pressure loss.
  • the structural elements can be arranged offset within a row, ie the Although structural elements are arranged in a row running transversely to the flow direction, they are staggered in the flow direction, which also results in the advantage of a lower pressure loss.
  • opposite rows ie one or the other side of the flat tube
  • can be staggered in the flow direction but there is always an overlap between the two rows. direction, there is less pressure loss. If the opposite structures touch and are connected by welding or soldering, the strength can be increased.
  • the structural elements are not arranged in a row at uniform intervals; rather, these rows have gaps which are opposite structural elements on the opposite side and thus “fill” these gaps - in plan view. This also gives the advantage achieved a lower pressure drop.
  • knobs and / or webs can also be stamped outwards or inwards (viewed in flow direction P) in order to achieve a "support” and thus an increase in strength.
  • the structures that produce vortices can also assume this function in whole or in part.
  • the essentially opposite heat transfer surfaces and in particular the structural elements arranged thereon are curved.
  • the advantages according to the invention are achieved in particular in the case of tubes with a circular or oval cross section.
  • the essentially opposite heat transfer surfaces are primary thermal surfaces.
  • the heat transfer surfaces are thermal secondary surfaces, which are formed in particular by ribs, webs or the like, preferably soldered, welded or clamped to the flow channel.
  • the height h of the structural elements is in the range from 2 mm to 10 mm, in particular in the range from 3 mm to 4 mm, preferably around 3.7 mm.
  • the flow channel is rectangular and has a width b which is in particular in the range from 5 mm to 120 mm, preferably in the range from 10 mm to 50 mm.
  • a hydraulic diameter of the flow channel is in the range from 3 mm to 26 mm, in particular in the range from 3 mm to 10 mm.
  • At least one, in particular each row of structural elements comprises a plurality of structural elements.
  • the aforementioned flow channels are provided as flat, round, oval or rectangular tubes of a heat exchanger, advantageously an exhaust gas heat exchanger.
  • the arrangement of the structural elements according to the invention that is to say advantageously their embossing into the inner tube walls, results in an increase in the performance of the heat exchanger.
  • the structural elements arranged in rows for exhaust gas heat exchangers are particularly advantageous because soot deposits are also avoided in the interior of the flat tubes.
  • a coolant flows around the outside of the exhaust gas pipes, which coolant circuit is taken from the coolant circuit of the internal combustion engine emitting the exhaust gases. It is also possible for the structures to be embossed in plates or disks in order to use them to produce heat exchangers. Exemplary embodiments of the invention are shown in the drawings and are described in more detail below. Show it
  • FIGS. 2a, b, c show a cross section of flow channels
  • FIG. 4 shows a half-shell of the flat tube according to FIG. 3,
  • FIG. 1 shows a simplified representation of a flow channel 1, which is designed as a rectangular tube, has a rectangular inlet cross section 2, two opposite flat sides F1, F2 and two opposite narrow sides S1, S2.
  • the channel 1 is from a flow medium, for. B. flows through an exhaust gas in the direction of arrow P.
  • V-shaped vortex generators 3a, 3b, 4a, 4b are arranged on the lower flat side F2, which produce increased turbulence of the flow by generating vortices and at the same time prevent soot deposition in the case of an exhaust gas flow.
  • This representation corresponds to the prior art mentioned at the beginning.
  • the vortex generators 3a, 3b and 4a, 4b which are arranged in pairs in a V-shape and widen in the direction of flow, are also referred to as winglets.
  • 2a shows the cross section of a flow channel 1 designed as a flat tube, in which winglet pairs 5a, 5b and 6a, 6b are arranged both on the upper flat side F1 and on the lower flat side F2.
  • the channel cross section has a channel height H and a channel width b.
  • the winglets 5a, 5b, 6a, 6b have a height h projecting into the channel cross section. This arrangement of winglets also corresponds to the prior art mentioned at the beginning.
  • the designations F1, F2 also apply to the following exemplary embodiments according to the invention.
  • FIG. 2b shows the cross section of a flow channel 1 ′ designed as a round tube, in which structural elements 13 ′ and 13 are arranged both on the upper flat side F1 and on the lower flat side F2.
  • the channel cross section has a channel height H.
  • FIG. 2c shows the cross section of a flow channel 1 designed as a flat tube, in which the heat transfer surfaces F1, F2 represent secondary surfaces in terms of heat technology, since they do not directly transfer heat from one medium to the other.
  • the heat transfer surfaces have structural elements 13, 13 '.
  • Fig. 3 shows a flow channel according to the invention, which is designed as a flat tube 7, which is partially shown in a plan view.
  • the flat tube 7 has a longitudinal axis 7a, a width b and two rows 8, 9 of structure elements or winglets 10, 11 arranged in a V-shape, each of which is embossed both in the top side F1 and in the bottom side F2 of the flat tube 7, and with the same pattern, so that the winglet row above coincides with the row below.
  • Eight winglets are arranged in a row, evenly distributed over the entire width b - however, there can also be six or seven winglets with the same width.
  • the number of winglets can also be below six wider pipes or discs / plates also above eight.
  • the two rows 8, 9 are at a distance s from one another which is measured from center to center and is approximately 2 to 6 times the length of the winglets. There is a smooth area between the individual rows, in which support structures are stamped, for example.
  • the rows of winglets extend over the entire length of the flat tube 7, in each case with the distance s, on both sides of the flat tube 7.
  • the half-shell 7b has a base F2 and two side legs 7c, 7d, with winglets on the base and the underside F2 11 'arranged, i. H. are stamped into the pipe wall.
  • the upper half-shell is not shown; it is a mirror image and is longitudinally welded to the lower half-shell 7b on the side legs 7c, 7d.
  • the winglets 1 ′ have a height h with which they protrude into the clear cross-sectional area of the flat tube 7.
  • the tube can also be made from sheet metal that is formed and welded on one side.
  • the width b of the flat tube is 40 mm or 20 mm
  • the total height of the flat tube is approximately 4.5 mm
  • the height h of the winglets is approximately 1.3 mm.
  • the clear cross-sectional height of 1.4 mm for a core flow remains as a result of the winglets, each 1.3 mm high, projecting into the channel cross section from both sides.
  • the distance s between the rows is approx. 20 mm.
  • the flat tube 7 is preferably used for exhaust gas heat exchangers known per se (not shown), that is to say exhaust gas from an internal combustion engine of a motor vehicle flows through on the inside and exhaust gas from a coolant circuit of the internal combustion engine flows through on the outside. engine cooled.
  • the outside of the flat tubes 7 - as is known from the prior art - can be smooth and can be kept at a distance from adjacent tubes, for example by embossed knobs. However, it is also possible to provide 7 ribs on the outside of the flat tubes to improve the heat transfer on the coolant side.
  • FIGS. 5a, 5b, 5c and 5d show individual structural elements which are provided for a structure according to the invention on the flow channels.
  • 5a shows an elongated structural element 13 with a longitudinal axis 13a, which forms an angle ⁇ , the outflow angle, with a reference line q.
  • the direction of flow for all representations 5a to 5d is the same in each case and represented by an arrow P.
  • the reference line q runs perpendicular to the flow direction P.
  • the structural element 13 has a length L and a width B. The latter can be constant or variable, i. H. towards P increasingly.
  • FIG. 5b shows an elongated but angled structural element 14 with two longitudinal axes 14a, 14b which are inclined towards one another and which each enclose an angle ⁇ and ⁇ with the reference line q, ⁇ is referred to here as the inflow angle and ⁇ as the outflow angle.
  • the flow according to arrow P is thus diverted in two stages, i. H. only slightly at first and then stronger. This results in a lower pressure drop - in comparison to a structural element according to FIG. 5a with the same outflow angle ⁇ .
  • the length of the structural element 14 along the longitudinal axes 14a, 14b is designated by L.
  • 5c shows an arcuate structural element 15 with a curved longitudinal axis 15a, which corresponds to an arc of a circle with the radius R.
  • the upstream angle is called the incident angle ß and the downstream the downward angle is referred to as the outflow angle ⁇ .
  • This continuously increasing deflection of the flow also results in a lower pressure loss - in comparison to the structural element 13 according to FIG. 5a.
  • the length of the structural element 15 along the longitudinal axis 15a is designated by L.
  • FIG. 5d shows a further embodiment of a structural element 16, which is of approximately Z-shaped design and also has a Z-shaped longitudinal axis 16a.
  • the inflow angle is designated by ⁇ , the outflow angle by ⁇ , it corresponds to a flow deflection of (90 ° - ⁇ ), which takes place in the central region of the structural element 16.
  • the inflow and outflow of this structural element occurs practically in the flow direction P. This results in a particularly low-pressure deflection of the flow.
  • the length of the structural element along the longitudinal axis 16a is designated by L.
  • 6a, 6b, 6c, 6d, 6e, 6f, 6g, 6h show arrangement patterns of the structural elements 13 according to FIG. 5a, namely in rows on a section of a flow channel. In the case of exemplary embodiments that are not shown, only individual structural elements lie opposite one another.
  • FIG. 6a shows the elongated structural elements 13 each arranged in two rows 17, 18, which are at a distance s in the flow direction P.
  • the structural elements 13 shown in solid lines are embossed in the upper side F1 of the flow channel.
  • Structured elements 13 ', shown broken, are also arranged in rows 19, 20 in the lower heat exchanger surface or side F2 of the flow channel.
  • the rows are shown by dashed lines.
  • the structural elements 13 'on the lower surface F2 are oriented opposite to the structural elements 13 on the upper surface F1, ie they have an opposite outflow angle ⁇ (cf. FIG. 5a).
  • the rows 19, 20 are offset from the rows 17, 18 in the direction of flow P, namely by the amount f.
  • the structural elements 13 and 13 'and the associated rows 17, 18, 19, 20 each have a depth T, ie an extension in the flow direction P.
  • the offset f is smaller than the depth T, so that between the rows 18, 20 or 17, 19 an overlap Ü remains, which results from the difference between T and f.
  • An offset of the rows 17, 19 or 18, 20 lying opposite each other advantageously results in a lower pressure loss than in rows without an offset.
  • FIG. 6b shows another pattern of structural elements 13 arranged in rows in a row 21 and a row 22 with different outflow angles ⁇ (not shown).
  • the structural elements 13 in solid lines are embossed in the upper side F1 of the flow channel.
  • On the lower surface F2 of the flow channel, in the flow direction P, structural elements 13 'shown in dashed lines at the same height are arranged with opposite orientations, so that an upper structural element 13 and an opposite lower structural element 13' each appear as a cross in plan view.
  • the upper row with structural elements 13 is thus not offset from the lower row with structural elements 13 '; the overlap Ü is 100%.
  • 6c to 6h show further arrangement patterns of the structural elements 13, 13 'on the upper (shown in solid lines) and the lower (shown in broken lines) side F1, F2 of the flow channel.
  • 6h also shows support elements 13 ′′ on the outside of the flow channels, which in this exemplary embodiment are arranged adjacent to the structural elements 13, 13 ′ and in particular within the rows formed by the structure elements 13, 13 ′.
  • the support elements in FIG For a desired support of the respective flow channel, the support elements 13 "advantageously have a height which corresponds to the desired distance between two flow channels or between the respective flow channel and a housing wall of a heat exchanger.
  • FIGS. 7a and 7b show further variants for the arrangement of the structural elements 13 in rows.
  • FIG. 7a shows a section of a flow channel with two rows 23, 24 of structural elements 13 arranged in a V-shape on the top side F1.
  • the structural elements 13 are not arranged next to one another at constant intervals, rather they have gaps 25, 26, 27, which, however, are filled on the underside F2 by structural elements 13 ', so that in the top view there is a continuous, uniform arrangement of structural elements 13 and 13 'results.
  • This arrangement of "incomplete" rows 23, 24 and the corresponding rows on the underside results in a lower pressure drop for the flow in the direction P, because the structural elements - seen in the width direction - only engage in the flow alternately from above and below.
  • FIG. 7b shows a similar, incomplete arrangement of parallel aligned structural elements 13 on the top side F1 in rows 28, 29.
  • the gaps between the structural elements 13 are in turn filled by structural elements 13 ′ on the underside F2, the structural elements 13 opening up the top side F1 and the structural elements 13 'on the bottom side F2 to form a zigzag arrangement in the top view.
  • This arrangement is also relatively low in pressure loss.
  • FIG. 8 shows a further embodiment for the arrangement of structural elements 13 and 13 'in two rows 30, 31 on the top side F1.
  • the structural elements 13 of the row 30 and the structural elements 13 'of the opposite row (on the underside F2) are arranged in parallel and at the same distance from one another.
  • the structural elements 13 can likewise be replaced by structural elements 14 (in FIG. 5b), 15 (FIG. 5c) or 16 (FIG. 5d). It would also be possible to use different structural elements, e.g. B. 13 and 14 to use.
  • 9a, 9b, 9c, 9d show variants of the structural elements 13, 14, 15, 16 by mirroring: This results in so-called winglet pairs 32, 33, 34, 35, a minimum distance a being provided between two structural elements ,
  • the direction of flow is generally in the direction of arrow P, the flow to the winglet pairs conventionally taking place at the narrowest point a.
  • These winglet pairs can be arranged side by side in rows, e.g. B. as in Figures 6 to 8.
  • 10a, 10b, 10c, 10d show further variations of the structural elements 13, 14, 15, 16 by parallel displacement. This results in double elements 36, 37, 38, 39 with equal distances a on the inflow and outflow side, the z. B. can be integrated into the structures according to FIGS. 6 to 8.
  • the structural elements of a row above and / or below do not necessarily have the same geometric shape or dimensions, as is shown by way of example with four structural elements in FIG. 11a. Rather, as shown in FIG. 11 b, the structural elements can be arranged with an offset f in the flow direction P.
  • FIG. 11c the outflow angles of the structural elements 13 vary, and in FIG. 11d the lengths L1, L2 of the structural elements 13 vary.
  • a combination (not shown) of the variants according to FIGS. 11b, 11c, 11d is also possible. These variations can also occur in the upper and / or lower surface F1 or F2.
  • FIG. 12a shows a further structural element 43, which is designed as an angle with two straight legs 43a, 43b, which are connected at their apex by an arc 43c.
  • this structural element 43 represents a modification of the pair of winglets 32 according to FIG. 9a.
  • the inflow preferably takes place in the direction of the apex 43c, corresponding to the arrow P.
  • FIG. 12b shows a further modification of the pair of structural elements 34 according to FIG. 9c, namely a structural element 44 with two curved legs 44a, 44b, which are connected at the apex by an arc 44c.
  • the structural element 44 which is likewise flowed toward in the direction of the apex 44c in accordance with the arrow P, initially causes a slight flow deflection, which is then reinforced due to the legs 44a, 44b that are curved into the flow.
  • the elements according to FIGS. 12a and 12b can be used in all the arrangements shown above, where two structures arranged in a V-shape can be found again.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

L'invention concerne un canal d'écoulement d'un dispositif de transfert de chaleur, comprenant deux surfaces de transfert de chaleur (F1, F2) disposées parallèlement à une distance correspondant à une hauteur de canal H. Chacune de ces surfaces de transfert de chaleur (F1, F2) présente une structure constituée d'une pluralité d'éléments structurels disposés les uns à côtés des autres en séries perpendiculairement au sens d'écoulement P et s'étendant à l'intérieur du canal d'écoulement, lesdits éléments structurels présentant chacun une largeur B, une longueur L, une hauteur h, un angle de flux sortant alpha et un chevauchement U, ainsi qu'un axe longitudinal.
EP04786965.6A 2003-10-28 2004-09-20 Canal d'ecoulement pour dispositif de transfert de chaleur et dispositif de transfert de chaleur comprenant de tels canaux d'ecoulement Expired - Lifetime EP1682842B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP10181882.1A EP2267393B1 (fr) 2003-10-28 2004-09-20 Canal d'écoulement pour un échangeur de chaleur

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10350418 2003-10-28
PCT/EP2004/010516 WO2005052490A1 (fr) 2003-10-28 2004-09-20 Canal d'ecoulement pour dispositif de transfert de chaleur et dispositif de transfert de chaleur comprenant de tels canaux d'ecoulement

Related Child Applications (2)

Application Number Title Priority Date Filing Date
EP10181882.1A Division-Into EP2267393B1 (fr) 2003-10-28 2004-09-20 Canal d'écoulement pour un échangeur de chaleur
EP10181882.1A Division EP2267393B1 (fr) 2003-10-28 2004-09-20 Canal d'écoulement pour un échangeur de chaleur

Publications (2)

Publication Number Publication Date
EP1682842A1 true EP1682842A1 (fr) 2006-07-26
EP1682842B1 EP1682842B1 (fr) 2014-06-04

Family

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EP04786965.6A Expired - Lifetime EP1682842B1 (fr) 2003-10-28 2004-09-20 Canal d'ecoulement pour dispositif de transfert de chaleur et dispositif de transfert de chaleur comprenant de tels canaux d'ecoulement
EP10181882.1A Expired - Lifetime EP2267393B1 (fr) 2003-10-28 2004-09-20 Canal d'écoulement pour un échangeur de chaleur

Family Applications After (1)

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EP10181882.1A Expired - Lifetime EP2267393B1 (fr) 2003-10-28 2004-09-20 Canal d'écoulement pour un échangeur de chaleur

Country Status (9)

Country Link
US (2) US20070107882A1 (fr)
EP (2) EP1682842B1 (fr)
JP (1) JP2007510122A (fr)
KR (1) KR20060101481A (fr)
CN (1) CN1875240B (fr)
BR (1) BRPI0415965B1 (fr)
DE (1) DE102004045923A1 (fr)
ES (1) ES2496943T3 (fr)
WO (1) WO2005052490A1 (fr)

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DE102007036308A1 (de) * 2007-07-31 2009-02-05 Behr Gmbh & Co. Kg Rippe für einen Wärmetauscher
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US20120067557A1 (en) 2012-03-22
WO2005052490A1 (fr) 2005-06-09
EP2267393A2 (fr) 2010-12-29
ES2496943T3 (es) 2014-09-22
JP2007510122A (ja) 2007-04-19
CN1875240A (zh) 2006-12-06
BRPI0415965A (pt) 2007-01-23
CN1875240B (zh) 2010-10-13
DE102004045923A1 (de) 2005-05-25
EP1682842B1 (fr) 2014-06-04
US20070107882A1 (en) 2007-05-17
EP2267393A3 (fr) 2012-07-04
EP2267393B1 (fr) 2017-06-28
BRPI0415965B1 (pt) 2018-06-12
KR20060101481A (ko) 2006-09-25

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