WO1999024772A1 - Heat exchanger - Google Patents

Heat exchanger Download PDF

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Publication number
WO1999024772A1
WO1999024772A1 PCT/GB1998/003368 GB9803368W WO9924772A1 WO 1999024772 A1 WO1999024772 A1 WO 1999024772A1 GB 9803368 W GB9803368 W GB 9803368W WO 9924772 A1 WO9924772 A1 WO 9924772A1
Authority
WO
WIPO (PCT)
Prior art keywords
plate
plates
plates according
ridge
edge regions
Prior art date
Application number
PCT/GB1998/003368
Other languages
English (en)
French (fr)
Inventor
Martin Booth
Barry Borgi
Edward Rodney Beldon
Original Assignee
Marconi Communications, Inc.
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 Marconi Communications, Inc. filed Critical Marconi Communications, Inc.
Priority to EP98952902A priority Critical patent/EP1029215A1/en
Priority to CA002309862A priority patent/CA2309862A1/en
Priority to BR9814170-8A priority patent/BR9814170A/pt
Priority to KR1020007005129A priority patent/KR20010015811A/ko
Priority to AU10444/99A priority patent/AU1044499A/en
Publication of WO1999024772A1 publication Critical patent/WO1999024772A1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0037Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/02Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the heat-exchange media travelling at an angle to one another
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations

Definitions

  • This invention relates to a plate-type heat-exchanger and a plurality of plates for a heat exchanger. It relates particularly, but not exclusively, to a heat exchanger for supplying cool fluid such as air to an electrical equipment cabinet .
  • Plates heat exchangers generally comprise a stack of thin plates which are typically four sided.
  • the plates are stacked to form a three dimensional structure in which cool external air and warm extracted air traverse opposite sides of each plate to allow exchange of heat.
  • the flow of cool air on one side of a plate is roughly at right angles to the flow of warm air across the other side of the plate.
  • Travelling down one side of the stack the edges of the plates are usually sealed together in pairs.
  • the edges of the plates are also sealed together in pairs but in an inverted arrangement so that where one plate is sealed to its upper neighbour along one edge on one side of the stack, it is sealed to its lower neighbour along another edge on an adjacent side of the stack. This allows cross-flow of warm air and cool air on opposite sides of each plate, the two flows typically remaining unmixed.
  • the heat exchanger plates are typically formed from metal such as aluminum or copper which are good heat conductors.
  • metal plates are, however, expensive to manufacture and difficult to assemble into stacks for heat exchangers particularly because of the necessity of forming seals between the edges of alternating pairs of plate edges. This results in a lengthy and awkward assembly process. Moreover, such plates are also vulnerable to corrosion and can be heavy.
  • Plastic plates have been developed to alleviate the problem of corrosion. Such plastic plates may also be difficult and time-consuming to assemble.
  • the plates, whether plastic or metal, are typically welded or glued to seal the edges together in the required manner, for example, to allow cross-flow.
  • a plurality of stackable plates for a heat exchanger which, when stacked one upon the other, form fluid channels between adjacent plates allowing heat exchange between fluid flowing on one side of a plate and fluid flowing on the other side of the same plate, each plate comprising interengaging means on at least one pair of opposing edge regions for engaging with interengaging means on a corresponding pair of edge regions of a neighbouring plate to form seals between these edges when the plates are stacked together.
  • one or both fluids are gaseous such as air.
  • the interengaging members are arranged so that when the plates are stacked together with directions of the fluid flow on opposite sides of any one plate cross .
  • the interengaging means comprises an elongate member extending along an edge region.
  • At least one pair of opposing edge regions are offset at a higher level with respect to a central region of at least one plate.
  • At least one pair of opposing edge regions is offset at a lower level with respect to a central region of at least one plate.
  • every other plate has edge regions which are at substantially the same level as a central region of the plate.
  • each plate is identical .
  • every other plate may be identical, there being two kinds of plates .
  • the interengaging means comprises a ridge along the edge regions projecting from one surface so as to form a recess on the other surface for accommodating a corresponding ridge on an adjacent plate so that a seal is formed between the plates along that edge region when the plates are stacked together.
  • each edge region of each plate comprises at least one such ridge along it .
  • one or more edge regions comprise two or more of the ridges spaced apart from one another.
  • the ridges form a substantially continuous ridge structure about the periphery of the plate.
  • each ridge is of the same cross section.
  • the cross section is constant along the ridge.
  • the cross section of the ridges is generally rectangular or generally square.
  • the width of the uppermost surface of the ridge is greater than that of the base of the ridge.
  • the sides of the ridge may be angled with respect to the plate in opposite directions so that the uppermost surface of the ridge is wider than the base of the ridge. These sides may be straight.
  • the resilience of the ridges of neighbouring plates enables one ridge to be snap-fitted into the ridge of the neighbouring plate.
  • At least one pair of opposing edge regions of each plate comprises a projection from one surface of the edge region for preventing the interengaging means on that surface of the plate from engaging with corresponding interengaging means on a neighbouring plate adjacent that surface of the edge region.
  • interengaging means on one or more edge regions in the form of two ridges are provided and in which the projections are positioned in between the ridges .
  • each plate has an interengaging corner structure for interengaging with a corresponding corner structure on a neighbouring plate.
  • a corner structure comprises a projecting member on one surface of the plate and a recess on the other surface of the plate.
  • the corner structures provide a means of locking plates together, via internal or external components such as clamps and so on.
  • a central region of the plate contains a plurality of upstands.
  • the upstands preferably protrude from one side of the plate, but upstands protruding from the other side of the plate may also be provided.
  • at least some of the upstands are lower than the separation of the central regions of the plates in the stack when the plates are stacked together.
  • one or more of the upstands comprise elongate recesses across an uppermost surfaces arranged to enable air to flow through the recess.
  • the elongate recesses are as deep as the height of some of the upstands.
  • the upstands may form part of the plate, for example, they may be formed by pressing the plate. Or, the upstands may be attached to the plate by gluing, welding or the like.
  • the opposing edge regions are substantially parallel to one another.
  • a heat exchanger comprising a plurality of plates according to the invention.
  • the heat exchanger comprises a plurality of identical plates.
  • a plurality of stackable plates for a heat exchanger which when stacked one upon the other, form fluid channels between adjacent plates allowing heat exchange between fluid flowing on one side of a plate and fluid flowing on the other side of the same plate, each plate being welded on at least one pair of opposing edge regions to a corresponding pair of edge regions of a neighbouring plate to form seals between those edges.
  • the weld is formed by sonic welding.
  • the plates are made from a polymeric material .
  • the heat-exchanger plates may comprise plastics or engineering polymers. Such plates have the advantage of being so inexpensive that they may simply be thrown away and replaced with new plates at regular intervals.
  • the plates may be an alloy of polymers and metal, whether ferrous or non-ferrous, or alloys of plastics, or metal, or a combination of both.
  • Figure 1 is a schematic plan view of a basic version of a heat exchanger plate in accordance with the invention.
  • Figure 2 is a schematic exploded cross-sectional view from the side of a stack formed from a number of plates like that seen in figure 1.
  • Figure 3 is a close-up schematic cross-sectional view mid-way along an edge of a stack of plates similar to the plate in figure 1.
  • Figure 4 is a close up schematic cross-sectional view mid-way along an edge of a stack of first and second improved plates in accordance with a preferred embodiment of the invention.
  • the dotted line shows an alternative improved version of one of the plates.
  • Figures 5A and 5C are schematic cross-sectional exploded views through improved ridges in the edge region of neighbouring plates according to the invention, the ridges being adapted to snap-fit into one another shown in figures 5B and 5D .
  • Figure 6 is a schematic perspective view from above of a first improved heat exchanger plate. The inserts show neighbouring edges of this first plate in cross-section.
  • Figure 7 is a schematic perspective view from above of a second heat exchanger plate.
  • Figure 8 is a side view of the corner region of plate 10A of figure 6 on top of plate 10B of figure 7, seen from the direction of arrow 110.
  • Figure 9 is a side view of the corner of plate 10A of figure 6 on top of plate 10B of figure 7 seen from the direction of arrow 120.
  • Figure 10 is a close up perspective view of upstands 45 and 50 showing air flow channel 60.
  • Figure 1 shows a basic heat exchanger plate in accordance with the principles of the invention.
  • a central region 2 is bounded by, in this embodiment, a continuous ridge of generally square cross-section 3.
  • Plate 1 is typically formed from injection moulding and ridge 3 is formed when a recess is pressed into the rear of plate 1.
  • Two opposite sides 3A of ridge 3 are at an approximately constant height along their length.
  • Pillars 4 are spaced at intervals part way along sides 3B. Pillars 4 which are taller than the ridge on which they are formed serve to space that ridge of one plate from a corresponding ridge of a neighbouring plate when the plates are stacked together to form a heat exchanger.
  • ridge 3A Midway between the outer edges of the lower plate 201 is ridge 3A which does not have any pillars 4. Therefore, there is nothing to prevent the recess at the rear of ridge 3B of plate 202 just above it from slotting over ridge 3A to form a seal at the side of the plate when the plates are stocked together.
  • ridge 3A slots into the recess behind ridge 3B on the plate just above it when the plates are stacked.
  • two pillars 4 midway across ridge 3B at the rear edge of plate 202 prevent ridge 3A of plate
  • each edge of each plate forms a seal with a corresponding edge region of one but not the other of its neighbouring plates in the stack.
  • FIG. 3 In which a cross-sectional side view through a mid portion of stack of four plates 101, 102, 103, 104 is seen.
  • the outermost edge of plate 101 forms a ridge 3A.
  • Ridge 3A slots into the recess formed to the rear of ridge 3B of plate 102.
  • ridge 3B also includes spaced upstanding projections 4 which prevent the recess to the rear of ridge 3A of plate 103 from slotting onto ridge 3B of plate 102. Therefore, fluid such as air can flow between plates 102 and 103 from left to right, or vice versa, as seen in the drawing. However, no fluids such as air can flow between plates 101 and 102 from left to right or vice versa because of the effective seal formed by the circuitous path provided between plates 101 and 102 where ridge 3A fits in the recess behind ridge 3B.
  • fluid such as air can flow between plates 101 and 102 in a transverse direction, ie into or out of the paper because of upstanding pillars 4 on the transverse edges of plate 101 (not shown) and upstands 60 which are periodically placed in the central region 2 of plate 101.
  • projections four are positioned so as to extend from ridges 3B on one surface of the heat exchanger plate
  • an alternative, or even an additional arrangement is such that the projections are placed on the rear surface of the plate, say below ridges 3A. Where both from and rear projections are provided, these would be on neighbouring edges of the same plate, though depending from opposite surfaces of that plate.
  • a further option is to provide two kinds of plates in the stack.
  • one or both kinds can be provided with an additional bend just inside the outer ridges 3A and 3B, formed in opposite directions, to enable the plates to sit more naturally upon each other.
  • plate 10B has a central section 26 which is lower than an edge region containing ridge 3A.
  • the edge region containing ridge 3A and central region 26 are separated by an intermediate region 27B.
  • plate 10A has a central region 26 which is generally higher than the edge region containing ridge 3B and upstands 4. Ridge 3B and central region 26 of plate 10A are separated by a region 27A, which is preferably, of the same dimensions as region 27B.
  • plate 10B is generally level over both edge and central regions as indicated by the dotted line in figure 4.
  • intermediate region 27B is at the same level as the remainder of plate 10B.
  • Other alternatives can be envisaged, for example, the inner edge of ridge 3A of plate 10B could extend below the level of the edge region. This would have the advantage of lengthening the undulating route between plates 10B and 10A, improving the degree of sealing. Additional ridges and recesses or other shapes can also be provided to lengthen and improve the route, the only requirement being that whatever shape is selected the structure is able to fit to the structure of a neighbouring plate to provide a seal .
  • the advantage of a structure chosen to sit within or on a neighbouring structure is one of simplicity.
  • ridges and recesses are especially simple to manufacture by injection moulding.
  • Plates 10B have a taller upstand 45 sized and shaped to sit within a recess formed to the rear of a lower upstand 50.
  • the interaction of upstands 45 and 50 space and support central regions 26 of plates 10A and 10B.
  • the upstands are typically recessed on their reverse side, both the upstands and recesses disturbing the air flow across the plate.
  • the upstands could simply be glued or welded to one or both surfaces of a plate.
  • the upstands cover around 3% (usually 3.11%) of the surface area of one side of the plate to provide the right degree of turbulence without excessive restriction of the flow.
  • the percentage area coverage of upstands can be varied between about 1 or 2% and 12%. For example, where the upstands are recessed on the other side of the plate, the effective area of the upstands doubles to around 6% of the area of the plate surface.
  • a ridge of initially square cross-section is pressed out by injection moulding. On cooling, the ridge deforms ever so slightly under its own weight, for example, or by an additional deformation force to produce a slight enlargement at the rear of recess 6.
  • press or zip lock structures such as those used to seal plastic folders are particularly suitable .
  • This method of forming ridges 3 in which natural deformation on cooling produces a snap- fit mechanism is particularly advantageous since no additional steps are required in producing the plates.
  • one major advantage of a preferred embodiment of the invention is that all the features necessary to provide the required airflow through the stack are formed in the plate on injection moulding without the need for further processing steps.
  • other processing steps may be introduced if desired, for example, if alternative snap-fit mechanisms are required.
  • Such alternative snap- fit mechanisms include press studs spaced about the outer and inner surfaces of neighbouring ridges or edge regions of the plates.
  • Another advantage is that on stacking the plates together, sealing of the plate edge in the required locations happens automatically as ridges slot into recesses up and down the stack. This dramatically reduces the construction time for a plate-type heat exchanger.
  • FIG. 5C and 5D A further type of ridge incorporating a snap- fit mechanism is shown in figures 5C and 5D.
  • the sides and uppermost surface of the ridge are flat, the sides being turned outwards from one another with respect to the main plate surface. In the embodiment shown the sides are at an angle of approximately 80° to the plate and the uppermost surface of the ridge.
  • ridges are not continuous around the plate but are bonded by corner recesses 20 and corresponding projections 22. Corner recesses 20 and projections 22 in conjunction with similar recesses on plate 10B, as will be described later, are used to locate plates 10A on 10B and 10B on 10A.
  • first heat exchanger plate 10A includes a recess 20 at each of its corners. Whilst a square plate is shown, and is preferred, a rectangular plate can be used. The walls of each corner recess 20 form projection 22, which depends from the underside of the plate 10A. Between each pair of corner recesses 20 are, in this embodiment, two substantially parallel ridges indicated at 3A and 3B. The parallel ridges 3A, 3B are formed along respectively edges 32, 34 and 36, 38 of the plate.
  • Upstands 40 are provided on opposite edges 36, 38 for separating one plate from its neighbour along those edges. Upstands 40 are spaced apart evenly along edges 36, 38 and are positioned in the gap between the substantially parallel ridges 30.
  • Upstands 45, 50 Two sets of centrally located upstands 45, 50 are also formed in the central region 26 of plate 10A.
  • Upstands 45 which project further than upstands 50, are provided for structural strength and plate separation. They also promote turbulence as do lower upstands 50.
  • Both upstands 45 and 50 have semi-cylindrical channels or ducts 60 formed across their upper surface for reducing form drag or stagnation ie the accumulation of material such as dust, particles, insects etc in the still air which forms behind any body when air or fluid flows around it.
  • the semi-cylindrical shape of channels 60 is seen in figure 10.
  • channels 60 are of almost the same depth as the height of the upstands. Nevertheless, the channels 60 can be varied in shape, size and orientation. Typically, the channels or recesses 60 are elongate though this is not necessary.
  • Upstands 45 and 50 are formed in alternate rows.
  • the shorter upstands 50 form the outermost row on all four edges.
  • the rows are aligned in this embodiment so that each upstand 45 is located substantially half way between two of the taller upstands 50.
  • the cross-sections AA' and BB ' shown in the inserts in figure 6 are through, respectively, edge region 32 and parallel ridges 30A and edge section 38 and parallel ridges 3B.
  • the two ridges are, in this particular embodiment, of approximately the same height and width as one another.
  • the main section of plate 26 is slightly lower than the level of edge section 32.
  • Region 27B just inward of parallel ridges 3A, 3B is the same level as the region between ridges 3A, 3B and the outer portion of edge section 32. This is also true for edge section 34.
  • edge sections 36 and 38 are slightly lower than central region 26.
  • section 27A which is just inward of ridges 3A 3B on edge sections 36 and 38 and edge sections 36 and 38 are positioned just below the level of the central section 26.
  • the height of ridges 30 is approximately a distance d above the base level of section 27A and 27B as appropriate. This means that relative to the central section 26 of plate 10A opposite edges 36, 38 are lower whereas opposite edges 32, 34 are higher.
  • lower edge sections 36, 38 engage plate 10B.
  • higher edge sections 32, 34 engage plate 10B.
  • FIG. 7 shows a second heat exchanger plate 10B according to the invention.
  • Plate 10B includes a recess 24 at each of its corners. Each recess 24 forms a projection 26, which depends from the underside of plate 10B. At one side of each recess 24 is a raised rectangular wall 28. Each recess 24 is spaced from its neighbouring corner recesses 24 by two substantially parallel ridges 3 (shown schematically only in figure 7) . Ridges 3 are formed on edge regions 40, 42, 44 and 46 and span the length between the raised walls 28, where present or corner recesses 24.
  • Upstands 4 are provided on edge regions 40, 42 of the plate 10B for plate separation. Upstands 4 are spaced apart evenly along the ends 40, 42 and are positioned in the gap between ridges 3.
  • a plurality of centrally located upstands 45, 50 are also formed on the central region 26 of plate 10B.
  • upstands 45 and 50 are provided for structural strength, plate separation and for turbulence promotion.
  • Both upstands 45 and 50 include channels 60 for reducing drag as shown in figure 10.
  • the upstands typically cover around 3% of one side of each plate in this case (or 3% of each side where the upstands are recessed) .
  • the upstands promote variation in fluid velocity, induce differential pressures across the plates so providing for turbulence in the flow.
  • Upstands 45 and 50 are also formed in alternating rows on plate 60, upstands 45 forming the outermost rows. Each projection 50 is positioned at a point substantially parallel to the midpoint between two projections 45. In other words the pattern of upstands on plate 10B is the reverse of that on plate 10A.
  • each pair of plates comprises a plate 10A and a plate 10B.
  • Figures 8 and 9 show how the plates 10A and 10B are aligned in each pair, in this case with 10A uppermost.
  • the projections 22 of the plate 10A are located in the corner recesses 24 of the plate 10B.
  • plates 10A and 10B in this manner creates a sandwich in which the edges of pairs of plates are sealed tightly together along opposite edges allowing airflow between intervening edges.
  • stacking the plates in this manner allows air to flow between a first and second plate in one direction and the second and a third plate in another, preferably transverse, direction.
  • the plates could be arranged and/or shaped so that air flow between a first and second plate is at an acute angle or even in a parallel direction with respect to air flow between the second and third plates, as would be understood by someone skilled in the art.
  • the heat-exchanger plates according to the present invention are preferably made from plastic material such as engineering polymers.
  • Engineering polymers yield plates which are durable yet cheap to produce.
  • the low cost of the plates means they can simply be thrown away and replaced with new ones when they become old or the heat transfer characteristics deteriorate due to particle build up. This is far simpler than the cleaning methods mandated by conventional arrangements.
  • the plates may be recycled to form new plates.
  • the present invention provides a heat-exchanger which is quick and easy to assemble.
  • a tight seal is provided between heat exchanger plates as the plates slot into one another at selected edges when stacked so that there is no need for sealing gaskets, gluing or welding.
  • the plates are arranged to provide a cross-flow or counter flow heat- exchanger, with unmixed flow.
  • interengaging members whilst preferably formed from interlocking structures such as a ridge/recess structure, they could be formed from a series of discrete neighbouring structures, though this is less preferred. These structures could be a series of shorter ridges interspersed with snap- fit mechanisms, or a series of discrete neighbouring snap-fit mechanisms such as press studs. Indeed, the interengaging members could simply be provided by substantially planar but offset edges of all or every other plate as these will provide a degree of sealing at the edges, for example, in figure 4 where regions 27A and 27B meet.
  • opposing edges of neighbouring pairs of plates may be welded together by sonic welding using sonitrodes.
  • Sonitrodes are typically made from steel having slightly roughened ends which grip a material to be welded.
  • the sonitrodes send a high frequency vibration into the material say at 95-150dB which agitates the material sufficiently to form a weld.
  • the frequency of the vibration is adjusted to the material to be welded as well as the length shape and strength of weld to be formed .
  • a minimum gap of 3mm between neighbouring plates is preferred, though not essential.
  • preferred embodiments of the plates have been found to withstand the pressure of 10 psi (pounds per square inch) before the seals between edges are compromised.

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  • 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)
  • Transformer Cooling (AREA)
PCT/GB1998/003368 1997-11-12 1998-11-12 Heat exchanger WO1999024772A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
EP98952902A EP1029215A1 (en) 1997-11-12 1998-11-12 Heat exchanger
CA002309862A CA2309862A1 (en) 1997-11-12 1998-11-12 Heat exchanger
BR9814170-8A BR9814170A (pt) 1997-11-12 1998-11-12 Transformador de calor.
KR1020007005129A KR20010015811A (ko) 1997-11-12 1998-11-12 열교환기
AU10444/99A AU1044499A (en) 1997-11-12 1998-11-12 Heat exchanger

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB9723812.5A GB9723812D0 (en) 1997-11-12 1997-11-12 Heat exchanger
GB9723812.5 1997-11-12

Publications (1)

Publication Number Publication Date
WO1999024772A1 true WO1999024772A1 (en) 1999-05-20

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Application Number Title Priority Date Filing Date
PCT/GB1998/003368 WO1999024772A1 (en) 1997-11-12 1998-11-12 Heat exchanger

Country Status (7)

Country Link
EP (1) EP1029215A1 (ko)
KR (1) KR20010015811A (ko)
AU (1) AU1044499A (ko)
BR (1) BR9814170A (ko)
CA (1) CA2309862A1 (ko)
GB (1) GB9723812D0 (ko)
WO (1) WO1999024772A1 (ko)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1114976A2 (de) * 1999-12-28 2001-07-11 ALSTOM POWER (Schweiz) AG Vorrichtung zur Kühlung einer, einen Strömungskanal umgebenden Strömungskanalwand mit wenigstens einem Rippenelement
WO2002014771A2 (de) * 2000-08-16 2002-02-21 Max Roth Wärmetauscher
US6364007B1 (en) 2000-09-19 2002-04-02 Marconi Communications, Inc. Plastic counterflow heat exchanger
US6660198B1 (en) 2000-09-19 2003-12-09 Marconi Communications, Inc. Process for making a plastic counterflow heat exchanger
WO2008113800A1 (de) * 2007-03-20 2008-09-25 ETA 86 Solar Steel AG Absorber für solarthermie und verfahren zur herstellung eines absorbers
US7591301B2 (en) 2005-09-13 2009-09-22 Catacel Corp. Low-cost high-temperature heat exchanger
US7594326B2 (en) 2005-09-13 2009-09-29 Catacel Corp. Method for making a low-cost high-temperature heat exchanger
US8047272B2 (en) 2005-09-13 2011-11-01 Catacel Corp. High-temperature heat exchanger
WO2011162659A1 (en) * 2010-06-24 2011-12-29 Alfa Laval Corporate Ab A heat exchanger plate and a plate heat exchanger
FR2989769A1 (fr) * 2012-04-19 2013-10-25 Valeo Systemes Thermiques Echangeur de chaleur.
EP3059518A3 (de) * 2014-12-03 2016-12-07 Robert Bosch Gmbh Absorber für einen kollektor, sowie kollektor
US20220010981A1 (en) * 2020-01-13 2022-01-13 The Regents Of The University Of California Low-drag, high-efficiency microchannel polymer heat exchangers

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100783616B1 (ko) * 2007-03-09 2007-12-07 충남대학교산학협력단 배기열 회수용 열교환기
KR102242186B1 (ko) 2019-10-14 2021-04-21 (주)화승코퍼레이션 판형 열교환기 및 이를 구비한 차량용 냉방시스템

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GB2063450A (en) * 1979-11-17 1981-06-03 Imi Marston Ltd Plate Heat Exchanger
WO1983001998A1 (en) * 1981-11-26 1983-06-09 Hallgren, Leif Heat exchanger plate
GB2158569A (en) * 1984-05-01 1985-11-13 Univ Birmingham A gas-to-gas heat exchanger
US4858685A (en) * 1982-12-06 1989-08-22 Energigazdalkodasi Intezet Plate-type heat exchanger
EP0464874A2 (en) * 1987-11-17 1992-01-08 Shinwa Sangyo Co., Ltd. Heat exchanger for cooling tower

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2063450A (en) * 1979-11-17 1981-06-03 Imi Marston Ltd Plate Heat Exchanger
WO1983001998A1 (en) * 1981-11-26 1983-06-09 Hallgren, Leif Heat exchanger plate
US4858685A (en) * 1982-12-06 1989-08-22 Energigazdalkodasi Intezet Plate-type heat exchanger
GB2158569A (en) * 1984-05-01 1985-11-13 Univ Birmingham A gas-to-gas heat exchanger
EP0464874A2 (en) * 1987-11-17 1992-01-08 Shinwa Sangyo Co., Ltd. Heat exchanger for cooling tower

Cited By (22)

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EP1114976A2 (de) * 1999-12-28 2001-07-11 ALSTOM POWER (Schweiz) AG Vorrichtung zur Kühlung einer, einen Strömungskanal umgebenden Strömungskanalwand mit wenigstens einem Rippenelement
EP1114976A3 (de) * 1999-12-28 2001-10-31 ALSTOM POWER (Schweiz) AG Vorrichtung zur Kühlung einer, einen Strömungskanal umgebenden Strömungskanalwand mit wenigstens einem Rippenelement
US6446710B2 (en) 1999-12-28 2002-09-10 Alstom (Switzerland) Ltd Arrangement for cooling a flow-passage wall surrrounding a flow passage, having at least one rib element
WO2002014771A2 (de) * 2000-08-16 2002-02-21 Max Roth Wärmetauscher
WO2002014771A3 (de) * 2000-08-16 2002-08-29 Max Roth Wärmetauscher
US6364007B1 (en) 2000-09-19 2002-04-02 Marconi Communications, Inc. Plastic counterflow heat exchanger
US6660198B1 (en) 2000-09-19 2003-12-09 Marconi Communications, Inc. Process for making a plastic counterflow heat exchanger
US8047272B2 (en) 2005-09-13 2011-11-01 Catacel Corp. High-temperature heat exchanger
US7591301B2 (en) 2005-09-13 2009-09-22 Catacel Corp. Low-cost high-temperature heat exchanger
US7594326B2 (en) 2005-09-13 2009-09-29 Catacel Corp. Method for making a low-cost high-temperature heat exchanger
EP2314951A1 (de) * 2007-03-20 2011-04-27 ETA 86 Solar Steel AG Absorber für Solarthermie und Verfahren zur Herstellung eines Absorbers
WO2008113800A1 (de) * 2007-03-20 2008-09-25 ETA 86 Solar Steel AG Absorber für solarthermie und verfahren zur herstellung eines absorbers
WO2011162659A1 (en) * 2010-06-24 2011-12-29 Alfa Laval Corporate Ab A heat exchanger plate and a plate heat exchanger
CN102985780A (zh) * 2010-06-24 2013-03-20 阿尔法拉瓦尔股份有限公司 热交换器板和板式热交换器
JP2013529770A (ja) * 2010-06-24 2013-07-22 アルファ・ラバル・コーポレイト・エービー 熱交換器プレートおよびプレート式熱交換器
AU2010356148B2 (en) * 2010-06-24 2013-10-17 Alfa Laval Corporate Ab A heat exchanger plate and a plate heat exchanger
CN102985780B (zh) * 2010-06-24 2015-04-01 阿尔法拉瓦尔股份有限公司 热交换器板和板式热交换器
US9534854B2 (en) 2010-06-24 2017-01-03 Alfa Laval Corporate Ab Heat exchanger plate and a plate heat exchanger
FR2989769A1 (fr) * 2012-04-19 2013-10-25 Valeo Systemes Thermiques Echangeur de chaleur.
EP3059518A3 (de) * 2014-12-03 2016-12-07 Robert Bosch Gmbh Absorber für einen kollektor, sowie kollektor
US20220010981A1 (en) * 2020-01-13 2022-01-13 The Regents Of The University Of California Low-drag, high-efficiency microchannel polymer heat exchangers
US12066197B2 (en) * 2020-01-13 2024-08-20 The Regents Of The University Of California Low-drag, high-efficiency microchannel polymer heat exchangers

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CA2309862A1 (en) 1999-05-20
AU1044499A (en) 1999-05-31
KR20010015811A (ko) 2001-02-26
GB9723812D0 (en) 1998-01-07
BR9814170A (pt) 2000-09-26
EP1029215A1 (en) 2000-08-23

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