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
  • F28F3/048—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 in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels
• • 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
  • F28D9/00—Heat-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
  • F28D9/0031—Heat-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
  • F28D9/0037—Heat-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
• • 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

Definitions

• This invention relates to heat exchangers and methods for their manufacture.
• it relates to "compact" heat exchangers which are characterised by high "area density”. This means that they have a high ratio of heat transfer surface to heat exchange volume.
• the plates and other components of a heat exchanger should be as uniform as possible, and straightforward to produce from standard machinery or standard components. Design features running in straight lines i.e. rectilinear, or on fixed radii are particularly desirable. This simplifies assembly and it is much cheaper to produce only a limited number of components than a huge variety. The designer is therefore constrained in his efforts to design a "distribution zone" which has a means of progressively adjusting the flow restrictions and hence the pressure drop as the fluid passes through a distribution zone. Flow restrictions associated with any particular movement of fluid through the distribution zone should ideally be decreased as the distance from the entry to the distribution zone increases.
• a heat exchanger comprising a plurality of plates bonded face-to-face one to the other, said plates having on their faces a plurality of upstanding fins defining therebetween passages for fluid flow, said heat exchanger having a main heat exchange zone and a distribution zone between the entry to the heat exchanger and the main heat exchanger zone, said plates similarly having a main heat exchanger zone and a distribution zone, there being upstanding fins in both said zones of said plates, said upstanding fins in the distribution zone of the plates comprising a plurality of discrete projections along the direction of fluid flow, characterised in that said discrete projections include amongst them a plurality of projections which are aligned differently from adjacent projections along the direction of fluid flow.
• the projections are typically created by photochemically or electrochemically etching (or by any other appropriate method) a network of discreet upstanding fins on one or both sides of said plates.
• the fluid passageways through the distribution zone are preferably interconnected, the interconnection being provided by spaces between said fins.
• side bars are typically created from unetched metal.
• the fins may be of variable length in the direction of fluid flow and offset at different angles to the overall flow direction of fluid through the heat exchange zone.
• the fins may comprise both rectilinear and curved projections.
• the fins may be straight-sided, curved or aerofoil-shaped or a combination of each. Where there are fins on both sides of the plates, the fins on one plate may register with identically configured fins on an adjacent plate and are joined together by e.g. brazing or diffusion bonding, or by the use of adhesives.
• the fin configuration etched onto one side of a particular plate may be identical to or different from that etched on an adjacent plate, or where a plate is etched on both sides, onto the other side of the same plate.
• Plane metal sheets may be used as separator plates with two or more finned plates to form one discrete flow layer for a single fluid.
• the designer of the distribution zone can vary the length of fins, the distance between them, (both along the flow direction and laterally of it), and the density of fins in a particular area of the distribution zone in the direction of fluid flow.
• the discrete projections, or fins, at the entry to the distribution zone may be positioned and angled such as to create a higher flow resistance to fluid which traverses a shorter path through the heat exchanger.
• Figure 1 is a schematic plan view showing a cross-section of a heat exchanger in accordance with the invention
• Figure 2 is a cut-away view of part of the heat exchanger of Figure 1 ;
• Figure 2 A is a cut-away view of part of an alternative heat exchanger;
• Figure 3 is a cross-section illustrating a principle of construction of the heat exchanger of Figure 2
• Figure 3A is a cross-section (similar to that of Figure 3) illustrating a principle of construction of the heat exchanger of Figure 2A
• Figure 4 is a schematic view, similar to Figure 1 , illustrating certain of the design characteristics of the heat exchangers according to the invention.
• a heat exchanger 10 (see Figure 1 ) has a main heat exchange zone 1 1 connected with a distribution zone 12 at its entry end.
• Heat exchanger 10 comprises a series of thin plates aligned parallel to one another, some of which are planar 14 and some of which 15 have a plurality of discrete projections or fins 16 and 17 extending towards plate 15. It is a plate of the type 15 (with projections or fins 16) which is seen in Figures 1, 2, 2A and 4.
• Plate 15 has fins 16 which extend parallel to one another along the line of flow (shown by arrow 18) through the main heat exchange zone.
• the distributor fins 17 may have some which are parallel to others but their alignment and location is determined by factors which will be described later in this document.
• Both types of fin 16 and 17 are photochemically or electrochemically etched from a sheet of parent metal e.g. stainless steel as are upstanding side bars or spacers 19 which are of the same height as the fins 16, 17. Fins 16, 17 and side bars 19 or spacers are etched on either both sides ( Figure 2) or one side only ( Figure 2 A) of plates 15. When both sides of a plate are etched, the fins are coincident with one another, such that they will register identically with fins 16, 17 and side bars 19 on adjacent plates 15 as seen in Figure 3. When etched on one side only, plate 15 may be stacked or shown in Figure 3 A.
• the side bars or spacers 19 extend around the periphery of plate 15 except for portions where an entry 20 and an exit 21 to the heat exchanger 10 are provided.
• the entry 20 is a side entry into the distribution zone 12 of heat exchanger 10 such that fluid passing through the heat exchanger 10 can enter at right angles to the direction of fluid flow through the main heat exchange zone 1 1.
• the exit 21 is similarly treated to permit fluid to exit at right angles to the flow through the main heat exchange zone 1 1.
• Fins 16, 17 are shown only in the portion of heat exchanger 10 adjacent entry 20, but in practice they extend throughout the heat exchanger.
• the junction between the distribution zone 12 and the main heat exchange zone 1 1 extends across the heat exchanger from the side 22 of entry 20 away from the end of the heat exchanger.
• the junction between the main heat exchange zone 1 1 and the exit distribution zone is shown by dashed line 23 in Figure 1. Side entry and exit configurations enable heat exchangers to be provided with multi-stream capability.
• Plates 14 and plates 15 which are etched on both sides are arranged in a stack, part of which is seen in Figure 3.
• a pair of etched plates 15 are arranged with their fins 16 and side bars 19 registered (Figure 3 illustrates a fin configuration in the main heat exchange zone 1 1 ).
• Planar plates (side plates 14) are added to provide a sandwich, or flow layer 30 which has enclosed passageways 30, all of which will carry the same fluid.
• An adjacent flow layer (not shown) can be built up parallel to that shown in Figure 3 and registering with its side bars 19. A different fluid will flow through the adjacent flow layer, and it may be that the fin pattern and distribution in adjacent flow layers may be different according to the fluid characteristics.
• the number of plates 15 making up a single flow layer may also be more than two.
• the entry and exit to the heat exchanger for different fluids are arranged to be from different sides of the heat exchanger, and this may be achieved by etching the entry and exit through the side bars 19 in different positions.
• An alternative build up of plates which are etched only on one side is shown in Figure 3A.
• the separation of the fins 17 in the distribution zones 12 (both along the overall flow direction and laterally of it) is generally not uniform, even at entry 20.
• the flow passageways in the distribution zones 12 which are created by the fins 17 are able to interact with each other by way of the spacings along the flow direction.
• Fins 16, 17 may be positioned anywhere on the surface of plate 15 where it is desired. As illustrated in this example, in the heat exchange zone 1 1 the fins 16 are arranged in rows in a regular pattern with alternate rows offset relative to each other i.e. the leading edge of each fin 16 in one row trails (or leads) the leading edge of each fin 16 in an adjacent row. The pitch of fins 16 may be such that the gap between fins along the flow direction is greater than the fin length. Each offset fin may then be more than a fin length behind the leading edge of a fin in an adjacent row. In the distribution zone 12, the fins 17 are arranged in lines which will curve towards the heat exchange zone 1 1.
• Alternate lines of fins 17 are then offset from one another in a similar way to the rows of fins 16 in the heat exchange zone 1 1.
• the offset fins, or some of them, may be angled differently from adjacent fins 17.
• the length of the fins 17 may be different at different positions in the distribution zone 12 e.g. the length may be greater as the flow approaches the heat exchange zone 1 1.
• the pitch of fins 17 may also change along their line through the distribution zone 12.
• supplementary fins 53, 54, 55 may be used to give a local higher fin density and to make small adjustments to the flow patterns to enhance even distribution of fluid across the whole of the heat exchange zone 1 1. Fins may be curved 40, aerofoil 41 or straight and they may be set at a variety of angles to the fluid flow.
• a typical distribution side entry could be designed such that the pitch and angle of fins 17 which are encountered by the fluid entering adjacent the point of entry 20 furthest from side 22, are such as to create a lower resistance to flow than the fins 17 (which are differently pitched and angled) encountered by fluid entering the distribution zone 12 closer to side 22 of entry 20. In this way a higher flow resistance may be created to fluid which takes a shorter path (e.g. arrow 51 - see Figure 4) than that which takes a longer path (e.g. arrow 52 - see Figure 4) through the heat exchanger 10.

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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)

Applications Claiming Priority (5)

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• 1997
  • 1997-03-26 WO PCT/GB1997/000848 patent/WO1997037187A1/en not_active Application Discontinuation
  • 1997-03-26 AU AU21691/97A patent/AU708247B2/en not_active Ceased
  • 1997-03-26 JP JP9535020A patent/JP2000506966A/ja active Pending
  • 1997-03-26 EP EP97914447A patent/EP0828983A1/en not_active Withdrawn
  • 1997-03-26 CA CA 2222716 patent/CA2222716A1/en not_active Abandoned

Non-Patent Citations (1)

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