Abstract: Two passages adjacent to each other via walls are formed spirally, and heat is exchanged between fluids passing through the passages via the walls. Upper and lower end faces of the spiral passages are covered with end plates, and the spiral passages and the end plates are sealed air-tightly. The end plates have a first passage inlet opening only to the first passage, a first passage outlet opening only to the first passage, a second passage inlet opening only to the second passage and a second passage outlet opening only to the second passage. Each of the inlets and outlets is open to every turn of the spiral passage. A first fluid entering the passage from the first passage inlet passes through the first passage for less than one turn only and is discharged from the first passage outlet. A second fluid entering the passage through the second passage inlet passes through the second passage for less than one turn only and is discharged from the second passage outlet.

Abstract: A liquid cooling device includes a casing (10) having a container (14) for accommodating liquid therein, and a liquid inlet port (18) in communication with the container (14). A funnel-shaped channel is defined in the liquid inlet port (18), and radiuses of the funnel-shaped channel are descended along a liquid flow direction.

Abstract: A cooling tower having a heat exchanger. The heat exchanger includes at least one heat exchanger pack having a generally diamond shape. The heat exchanger pack includes a first set of passageways for receiving a stream of warm, water laden air and a second set of passageways for receiving ambient air. The first set of passageways and second set of passageways are separate. Cooling tower configurations including the heat exchanger pack are disclosed for achieving effluent plume abatement, and capture of a portion of the effluent for replacement back into the cooling tower reservoir or as a source of purified water.

Abstract: A heat exchange unit includes metallic heat transfer members combined with each other. Each heat transfer member has a heat transfer face having opposite surfaces with which first and second heat exchange fluids come into contact, respectively. Welded-together flat portions of the heat transfer members are inserted into a fitting hole of an end plate. The fitting hole substantially coincides with an end shape of the combined heat transfer members and is sized to slidably receive welded-together flat portions such that the end plate and the received, welded-together flat portions contact each other. After insertion, the heat transfer members are welded to the end plate along the fitting hole so that, at the welded region, the heat transfer members and the end plate form an integral construction.

Abstract: A compact heat exchanger and/or fluid mixing means comprises a bonded stack of plates, the stack comprising at least one group of plates, the group comprising one or more perforated plates (10) sandwiched between a pair of primary separator plates (40, 62, 64), characterised in that each perforated plate (10) has perforations (14) arranged in rows across the plate in a first direction, with a land (16) between each adjacent pair of perforations (14) in a row and with ribs (18) between adjacent rows, the lands (16) forming barriers to flow in a first direction across the plate and the ribs (18) forming barriers to flow in a second direction across the plate, the second direction being normal to the first direction, the ribs (18) having vents (20) through a portion of their thickness, the vents (20) extending from one side of a rib (18) to the other side in the second direction, whereby flow channels are provided through the vents (20) and the flow channels lying between each adjacent pair of lands (16) provide

Abstract: A heat exchanger includes a container having an outlet and an entrance coupled to an inlet and an exit, a receptacle having an entering port and a discharging port for circulating a fluid medium and having an entering opening and a discharging opening. A casing is disposed between the container and the receptacle and includes a passage coupled between the outlet of the container and the entering opening of the receptacle, to allow a heat medium to flow from the container into the receptacle, and a chamber communicating with the discharging opening of the receptacle and the entrance of the container. An air filtering device may be disposed in the casing for air filtering purposes, and for collecting and discharging water.

Abstract: The efficiency of a heat exchanger is significantly improved by forming walls in an air flow structure, which has first grooves formed in the top surface of the structure and second grooves formed in the bottom surface of the structure, that block off alternating ends of the first and second grooves such that a first air source can only flow through the first grooves and a second air source can only flow through the second grooves.

Abstract: The invention refers to a heat exchanger plate (4) for a plate heat exchanger (1), a plate package (3) and a plate exchanger (1). The plate (4) includes at least a first area (31) with a corrugation of ridges and valleys, the plurality of which extends in a first direction (A), and at least a second area (32) with a corrugation of ridges and valleys, the plurality of which extends in a second direction (B). The plate (4) has a central rotary axis extending in parallel with a normal line of the plate. The areas (31, 32) have a respective contour coinciding with a respective imaginary contour in a first rotary position of the plate with regard to the rotary axis and after a rotation 90° to a second rotary position of the plate with regard to the rotary axis.

Abstract: A heat transfer member for a heat exchanger, is press-formed of a metallic thin sheet material into a prescribed shape by means of molds of a press forming device so that the heat transfer member has on at least one portion thereof a heat transfer face having opposite surfaces, which are to be brought into contact with heat exchange fluids, respectively. The heat transfer face comprises at least one set of irregularity patterns arranged in a row.

Abstract: A heat exchanger (50) is provided for transferring heat between first and second fluids (52) and (54) having a maximum operating mass flow rate through the heat exchanger (50) and mass flow rates that are substantially proportional to each other. The heat exchanger (50) provides essentially constant outlet temperatures for the first and second fluids (52,54) for all of the flow rates within the operating spectrum of the heat exchanger (50) without the use of an active control system. The heat exchanger (50) is of particular use in the fuel processing system (36) of proton exchange membrane type fuel cell systems.

Abstract: The invention refers to a heat exchanger plate (4) for a plate heat exchanger, a plate package, and a plate heat exchanger. The plate includes an edge, which extends around the plate, an edge area (6) which extends around the plate inside the edge, and a heat exchanging surface (5) with a corrugation of ridges and valleys which extend in at least a first direction (A, B) over the plate (4). Furthermore, the plate includes a support area (41), which extends around the heat exchanging surface (5) inside the edge area (6) and includes a corrugation of ridges (42) and valleys (43).

Abstract: The invention concerns an independent heat exchange unit designed to be fixed inside a building comprising a box provided with walls defining two fluid passages with an undulating cross-section and means for circulating air capable of causing countercurrent circulation in the two fluid passages of a fresh air stream drawn from outside the building and a stale air stream drawn from inside the building. The walls defining the fluid passages comprise a flexible and thin foil forming undulations capable of being deformed depending on the respective pressure levels of the fresh air stream and the stale air stream. The invention is useful for ventilating and/or air-conditioning the inside of buildings.

Abstract: A tube support device comprises an elongated strip inserted in a tube lane between the tubes of the tube bundle. Raised-tube-engaging zones are disposed in transverse rows across the strip at successive longitudinal locations along its length; these tube-engaging zones extend laterally outwards from both faces of the strip to engage with tubes on opposite sides of the tube lane. The tube-engaging zones may be arranged so that they extend from the two faces of the strip in an alternate manner, with the tube-engaging zones in each row alternately extending from one face and then from the other along the row.

Abstract: Two passages adjacent to each other via walls are formed spirally, and heat is exchanged between fluids passing through the passages via the walls. Upper and lower end faces of the spiral passages are covered with end plates, and the spiral passages and the end plates are sealed air-tightly. The end plates have a first passage inlet opening only to the first passage, a first passage outlet opening only to the first passage, a second passage inlet opening only to the second passage and a second passage outlet opening only to the second passage. Each of the inlets and outlets is open to every turn of the spiral passage. A first fluid entering the passage from the first passage inlet passes through the first passage for less than one turn only and is discharged from the first passage outlet. A second fluid entering the passage through the second passage inlet passes through the second passage for less than one turn only and is discharged from the second passage outlet.

Abstract: Disclosed herein is a heating system of floating floor structure including a heating panel with a circular or elliptical inner fluid pathway. The heating panel having the circular or elliptical inner fluid pathway overcomes limitation on pressure resistance, which is the problem of the convention heating panel having a hexagonal fluid pathway, thereby providing enhanced pressure resistance. Furthermore, a floating floor structure of the heating system enhances thermal efficiency, and effectively improves sound absorbing/dampening function in a floor of a building. Additionally, the floating floor structure is provided with inner spaces, which allow utility equipment, such as an electric wire or a pipe, to be easily established therein, thereby enabling an easy repair of the heating system and the utility equipment.

Abstract: The efficiency of a heat exchanger is significantly improved by connecting walls to an air flow structure, which has first grooves formed in the top surface of the structure and second grooves formed in the bottom surface of the structure, that block off alternating ends of the first and second grooves such that a first air source can only flow through the first grooves and a second air source can only flow through the second grooves.

Abstract: This invention relates to a process for cooling or liquefying a fluid product (e.g., natural gas) in a heat exchanger, the process comprising: flowing a fluid refrigerant through a set of refrigerant microchannels in the heat exchanger; and flowing the product through a set of product microchannels in the heat exchanger, the product flowing through the product microchannels exchanging heat with the refrigerant flowing through the refrigerant microchannels, the product exiting the set of product microchannels being cooler than the product entering the set of product microchannels. The process has a wide range of applications, including liquefying natural gas.

Abstract: Heat exchangers, constructed in accordance with principles of this invention, comprise a plurality of first passages, for transporting a first fluid or gas therethrough, and one or more second passages for transporting a second fluid or gas therethrough. The second passages are positioned adjacent to the first passages to permit a desired transfer of thermal energy from the first passages to the second passages. At least one manifold is placed in communication with one of the first or second passages. The manifold includes an opening disposed therethrough for receiving or dispensing the first or second fluid or gas to or from the first or second passages. The heat exchanger includes a flow director disposed therein for diverting or distributing the flow of first or second fluid or gas in a manner different from a natural fluid or gas flow within the heat exchanger.

Abstract: A fluid processing unit having first and second interleaved flow paths in a cross flow configuration is disclosed. The first flow paths are substantially longer than the second flow paths such that the pressure drop in the second flow paths can be maintained at a relatively low level and temperature variations across the second flow paths are reduced. One or more of the flow paths can be microchannels. When used as a vaporizer and/or superheater, the longer first flow paths include an upstream liquid flow portion and a downstream vapor flow portion of enlarged cross sectional area. A substantial pressure drop is maintained through the upstream liquid flow portion for which one or more tortuous flow channels can be utilized. The unit is a thin panel, having a width substantially less its length or height, and is manufactured together with other thin units in a bonded stack of thin metal sheets. The individual units are then separated from the stack after bonding.

Abstract: A heat transfer assembly is disclosed which comprises at least one wall (1, 2, 3) which is adapted to separate a first fluid at a first temperature from a second fluid at a second temperature, and at least one fiber member (6, 7, 8, 9) or plurality of them, each fibre member (6, 7, 8, 9) including at least one elongate fibre which extends substantially axially along the fiber member (6, 7, 8, 9) from the first fluid through the wall (1, 2, 3) and into the second fluid whereby in use heat is transferred from the first fluid to the second fluid or vice versa, and the entire heat transfer assembly or a part of it is assembled as a single unit by sewing/weaving/stitching technique.

Abstract: The ventilating system includes evaporative cooling of the exhaust air before it enters a heat exchanger to cool incoming fresh outside air. A suction fan pulls exhaust air through the heat exchanger and, in combination with a flow restrictor, reduces the pressure on the exhaust air and augments the evaporative cooling. The use of a pusher fan to force outside air through the heat exchanger ensures that any leakage in the heat-exchanger results in outside air entering exhaust air and minimizing the chances of contamination by leaking exhaust air into the incoming fresh air. The heat exchanger is made economically by heat-forming cavities in relatively thick thermo-plastic sheets, interleaving them with other thermoplastic sheets having separate gas flow conduit structures, and securing the sheets together. Preferably, the heat-exchanger is an opposed-flow heat-exchanger giving improved heat-transfer efficiency.

Abstract: The invention provides an improved heat exchanger of the so-called “pin-fin” type. The heat exchanger comprises a stack of parallel perforated plates, each plate of the stack having perforations, characterized in that the perforations define an array of spaced column precursors, of thickness equal to the plate thickness, the column precursors being joined together by ligaments, each ligament extending between a pair of adjacent column precursors, the ligaments having a thickness less than the plate thickness, the column precursors of any one plate being coincident in the stack with the column precursors of any adjacent plate whereby the stack is provided with an array of individual columns, each column extending perpendicularly to the plane of the plates, whereby fluid flowing through the stack is forced to follow a tortuous flow path to flow around the columns.

Abstract: A heat exchanger (10) is provided to transfer heat between a first and second fluid flow. The heat exchanger 10 includes a flow path (20) provided in the form of one or more heat exchange tubes (40, 40A-C), and a second flow path (30) provided in the form of one or more serpentine heat exchange tubes (42, 42A-C). The tube(s) (40, 40A-C) is (are) “woven” together with the tube(s) (42, 42A-C) such that they are perpendicular to each other. The heat exchanger (10) can provide particular advantages when used as a suction line heat exchanger in a transcritical cooling system (12).

Abstract: A compact ventilator with high efficiency thermal exchanger and a conveniently exchangeable air filter. The conveniently exchangeable filter enables a ventilator with thermal exchanger to be easily and regularly maintained and serviced, thereby enhancing its practical utility.

Abstract: A method for processing separate fluid flows in a micro component system for the production of hydrogen gas used in fuel cells in which a first fluid flow is directed to micro channels formed on one side of a conductive separator maintained in an enclosure, a second fluid flow is directed to micro channels formed on the opposite side of the separator, and laminar flow is maintained in the fluids such that heat transfer between the fluids on the opposite sides of the micro channels is by conduction through the separator and heat transfer within the fluids on the opposite sides of the micro channels is predominantly by convection within the fluids.

Abstract: A heat sink fan comprises a heat sink (2) including a base member (21) and a plurality of thin heat radiating fins (22) fixed thereto, and a fan case (1) for supporting an axial flow fan (18) that induces air flow for cooling the heat sink (2). The fan case (1) includes an upper wall portion (11), at least one pair of engaging portions (12) depending from side edges of the upper wall portion (11), and a protruding portion (13) formed at the substantial middle portion of both end portions in the longitudinal direction of the upper wall portion (11). A thickness of one or more heat radiating fins (2) facing to the protruding portion (13) is larger than a thickness of other heat radiating fins.

Abstract: A heat exchanger is made from a single piece of metal foil. The foil is coated with catalyst, corrugated with herringbone or skew corrugations, except along narrow flat areas near its edges, and folded back and forth upon itself. The folded metal structure is blocked off, except at regions near the flat areas, and enclosed in a container. A first gas stream flows into one set of folds, in a path which includes the flat areas and the channels formed by the corrugations. A second gas stream similarly flows into the other set of folds. The two streams are in thermal contact, but do not mix. The heat exchanger is especially useful in operating a catalytic fuel reformer, or in other applications involving catalytic processes. Alternative embodiments use straight corrugations to create straight channels that minimize the pressure drop through the heat exchanger.

Abstract: A bottom heat dissipating device may be attached to a bottom surface of a printed circuit board (PCB). A top surface of the bottom heat dissipating device may be thermally coupled with a backside surface of one or more electronic components mounted on the bottom surface of the PCB. A top heat dissipating device may be attached to a top surface of the PCB. The top heat dissipating device may be thermally coupled with the bottom heat dissipating device through a thermally conductive coupling member to provide a conductive path for heat transfer from the bottom heat dissipating device to the top heat dissipating device. An opening adjacent to an edge of the thermally conductive coupling member may allow air flow between the top and bottom heat dissipating devices. The PCB may be part of a mezzanine card, such as a Peripheral Component Interconnect (PCI) mezzanine card (PMC).

Abstract: An improved counterflow heat exchanger is described. The heat exchanger has one or more cold air intake passageways and one or more hot air intake passageways wherein the flow of cold air is opposite the flow of hot air. In addition, each cold air intake passageway contacts at least one hot air intake passage way.

Abstract: An extremely high efficiency, cross flow, fluid-fluid, micro heat exchanger and novel method of fabrication using electrode-less deposition is disclosed. To concurrently achieve the goals of high mass flow rate, low pressure drop, and high heat transfer rates, the heat exchanger comprises numerous parallel, but relatively short microchannels. Typical channel heights are from a few hundred micrometers to about 2000 micrometers, and typical channel widths are from around 50 micrometers to a few hundred micrometers. The micro heat exchangers offer substantial advantages over conventional, larger heat exchangers in performance, weight, size, and cost. The heat exchangers are especially useful for enhancing gas-side heat exchange. The use of microchannels in a cross-flow micro-heat exchanger decreases the thermal diffusion lengths substantially, allowing substantially greater heat transfer per unit volume or per unit mass than has been achieved with prior heat exchangers.

Abstract: A heat exchanger including inlet and outlet header portions for a refrigerant (such as CO2), serpentine multiport tubes each with a plurality of aligned tube runs, and at least three plate assembly fluid paths. Each plate assembly fluid path includes a pair of spaced plates secured together at their edges to define an enclosed space with a fluid inlet and fluid outlet on opposite sides of the space. One plate of one fluid path is positioned against first aligned tube runs, one plate of a second of the fluid paths is positioned against second aligned tube runs, and a third fluid path is positioned between the first and second aligned tube runs. The plates may be substantially identical to one another.

Abstract: The efficiency of a heat exchanger is significantly improved by forming walls in an air flow structure, which has first grooves formed in the top surface of the structure and second grooves formed in the bottom surface of the structure, that block off alternating ends of the first and second grooves such that a first air source can only flow through the first grooves and a second air source can only flow through the second grooves.

Abstract: Two passages adjacent to each other via walls are formed spirally, and heat is exchanged between fluids passing through the passages via the walls. Upper and lower end faces of the spiral passages are covered with end plates, and the spiral passages and the end plates are sealed air-tightly. The end plates have a first passage inlet opening only to the first passage, a first passage outlet opening only to the first passage, a second passage inlet opening only to the second passage and a second passage outlet opening only to the second passage. Each of the inlets and outlets is open to every turn of the spiral passage. A first fluid entering the passage from the first passage inlet passes through the first passage for less than one turn only and is discharged from the first passage outlet. A second fluid entering the passage through the second passage inlet passes through the second passage for less than one turn only and is discharged from the second passage outlet.

Abstract: A heat exchanger is made from a single piece of metal foil. The foil is coated with catalyst, corrugated with herringbone or skew corrugations, except along narrow flat areas near its edges, and folded back and forth upon itself. The folded metal structure is blocked off, except at regions near the flat areas, and enclosed in a container. A first gas stream flows into one set of folds, in a path which includes the flat areas and the channels formed by the corrugations. A second gas stream similarly flows into the other set of folds. The two streams are in thermal contact, but do not mix. The heat exchanger is especially useful in operating a catalytic fuel reformer, or in other applications involving catalytic processes. Alternative embodiments use straight corrugations to create straight channels that minimize the pressure drop through the heat exchanger.

Abstract: A plate cooler for cooling a fluid made of a plurality of superposed pairs of spaced plates sealed at their margins by side and end plates to form fluid flow channels and connected by lateral plates. The spaced plates and lateral plates are provided with aligned fluid flow openings forming a fluid flow conduit connected to a fluid input and output. The cooler is preferably made of aluminum or an aluminum alloy and is assembled by vacuum welding.

Abstract: A cooling device for cooling an inner part of an approximately sealed box includes a casing and a heat exchanger disposed in the casing. Plural inside air passages through which air inside the box flows and plural outside air passages through which air outside the box flows are alternately adjacently arranged in the heat exchanger. In the cooling device, both outside air introduction port and outside air discharge port are provided in an outer side plate of the casing, and a drain space is provided between the heat exchanger and the outer side plate of the casing so that outside air passages communicate with the outside air discharge port through the drain space. Thus, even when rain water is introduced into the casing from the outside air discharge port, almost rain water flows downwardly through the drain space, and it can restrict rain water from being introduced into the heat exchanger.

Abstract: An exhaust that has two isolated baffle systems in one container. This allows the exhaust from one manifold to be muffled and exhausted independently of the other manifold's exhaust. Moreover, the muffler is the same size as existing mufflers, so that it fits into the space of the prior art mufflers. Using two independent muffler elements (baffles and outer covering cans) eliminates all of the problems discussed above and increases the engine horsepower without reducing efficiency. An outer shroud covers the two muffler elements and is also designed to act as a heat exchanger. Fresh air can be pulled through the muffler to be heated for cabin heat and for carburetor heat. The shroud has space around the muffler cans, through which the fresh air passes. Inlet and outlet ports are provided to allow hoses to be connected as needed.

Abstract: A cylinder-type heat exchanger including cells spirally wound between an inner cylinder and an outer cylinder which are concentrically arranged. Each cell includes a first plate and a second plate which are in contact with each other. The first and second plates each have several inlets and outlets arranged in parallel at opposed ends in the axial direction, with communication portions being arranged between the inlets and between the outlets. A first flow passage through which a first fluid flows is formed on the confronting sides of the first plate and the second plate, while a second flow passage through which a second fluid flows is formed on the non-confronting sides of the first plate and the second plate.

Abstract: A plate heat exchanger includes a case assembly and a plurality of primary flow channel assemblies. The case assembly includes first and second side panels and first and second end plates mounted to the ends of the side plates. Each of the end plates has alternating slots, and ribs extending transversely between the laterally extending edges of the end plate, with the slots of the first end plate and corresponding slots of the second end plate defining multiple pairs of slots. Each primary flow channel assembly includes laterally spaced first and second heat exchange plates, with the inner surfaces of the heat exchange plates forming a longitudinally extending primary flow passage. One of the primary flow channel assemblies is associated with each pair of slots with a first end portion of the flow channel assembly mounted in the slot of the first end plate and the second end portion of the flow channel assembly mounted in the corresponding slot of the second end plate.

Abstract: A bottom heat dissipating device may be attached to a bottom surface of a printed circuit board (PCB). A top surface of the bottom heat dissipating device may be thermally coupled with a backside surface of one or more electronic components mounted on the bottom surface of the PCB. A top heat dissipating device may be attached to a top surface of the PCB. The top heat dissipating device may be thermally coupled with the bottom heat dissipating device through a thermally conductive coupling member to provide a conductive path for heat transfer from the bottom heat dissipating device to the top heat dissipating device. An opening adjacent to an edge of the thermally conductive coupling member may allow air flow between the top and bottom heat dissipating devices. The PCB may be part of a mezzanine card, such as a Peripheral Component Interconnect (PCI) mezzanine card (PMC).

Abstract: A reboiler/condenser bath heat exchanger for heat exchange between a first fluid to be vaporized and a second fluid to be condensed includes a number of passages for heat exchange between the two fluids in order to make the second fluid flow, which fluid has a temperature of T2-2 at the outlet of the passages; a vessel containing the passages for making the first fluid flow between the passages by thermosiphon effect from the bottom upwards over a height h, the first fluid having an entry temperature T1-1 where T1-1<T2-2 and an exit pressure P1-2; elements for giving the entry pressure P1-1 of the first fluid a value such that the pressure P1-2 is greater than a minimum pressure Pm,ex and elements for ensuring that at least one of the following two conditions is fulfilled: the height h of the passages is at least equal to 2.5 m; and the temperature T2-2 of the second fluid is less than T1-1+1.2° C.

Abstract: A corrugated fin for a composite heat exchanger for motor vehicles include a condenser portion and a radiator portion. The radiator portion is larger in fin width than the condenser portion. The condenser portion and the radiator portion have respectively first and second louvers formed corresponding to the fin widths. The first and second louvers respectively have first and second louver slats inclined in a direction which is different for each of the condenser portion and the radiator portion to oppose each other, and an inclination angle of the second louver slats is smaller than an inclination angle of the first louver slats.

Abstract: An arrangement for a fluid distributor-contactor-type reactor uses perforated plates to circulate two reactants in alternate channels defined by spaces between parallel stacked plates to perform controlled distribution and mixing simultaneously with optional indirect heat transfer. One reactant enters one set of channels that serve as reaction channels. A set of second channels interleaved with the reaction channels serve as distribution channels that also provide a heat exchange function. Finely dispersed openings in the perforated plates distribute the reactant at low concentration from the distribution channels into the reaction channels. Dispersal of the reactant through the perforations will enhance the turbulence that is primarily introduced by the corrugated plates to insure good mixing of the reactants in the reaction channels.

Abstract: A heat exchanger (10) is provided to transfer heat between a first and second fluid flow. The heat exchanger 10 includes a flow path (20) provided in the form of one or more heat exchange tubes (40, 40A-C), and a second flow path (30) provided in the form of one or more serpentine heat exchange tubes (42, 42A-C). The tube(s) (40, 40A-C) is (are) “woven” together with the tube(s) (42, 42A-C) such that they are perpendicular to each other. The heat exchanger (10) can provide particular advantages when used as a suction line heat exchanger in a transcritical cooling system (12).

Abstract: Heat exchanger core including flat plate parts formed by alternately folding back a single belt-like metal plate in a zigzag fashion at a first fold-back edge and at a second fold-back edge; element parts formed by joining peripheral edges of a pair of adjoining flat plate parts which are integrally coupled to each other at the first fold-back edge and adjoining element parts are integrally coupled at a certain interval to each other at the second fold-back edge; and a pair of ports for a first fluid formed at positions apart from each other at the peripheral edge of each element part. A second fluid flows along the outer surface side of each element part.

Abstract: A double sided-double heat exchanger core includes a plurality of sets of fluid passageways separated by a plurality of “S” shaped thermally conductive walls. Each set includes a plurality of fluid passageways. Each thermally conductive wall is configured to separate fluid flow between adjacent sets and configured to separate fluid flow between fluid passageways of one of the adjacent sets. The heat exchanger core is configured to provide segregated fluid flow between adjacent sets of fluid passageways. This heat exchanger core is particularly applicable for cooling equipment cabinets, wherein the air used to cool the equipment is recirculated through a plurality of sets and ambient air flows through interlaced sets to cool the recirculated air.

Abstract: A plate heat exchanger for indirect heat exchange of several fluid flows (30, 40, 50) with a heat transfer medium/cooling medium (10, 20) in a heat exchanger core (9) has a plurality of heat exchange passages within the core for the heat transfer medium/cooling medium (10, 20), a first fluid flow (30, 40, 50) and a second fluid flow (30, 40, 50). All heat exchange passages for the first fluid flow (40) are located In a first component area, and all heat exchange passages for the second fluid flow (30) are located in a second component area. The first and the second component areas do not intersect and each extend over the entire height of the heat exchanger core (9). The heat exchanger is particularly suitable for use in air-separation processes.

Abstract: Outsides of flat tubes through which a first fluid flows are formed with wave-shaped surfaces, and fins form meandering passages for a second fluid. While the second fluid is flowing along the fins, it is made turbulent by striking the wave-shaped surfaces of the flat tubes due to the meandering passages. The turbulent flow contacts the outside surfaces of the flat tubes and the front and rear surfaces of the fins, so heat conduction is promoted without the formation of thick boundary layers at these surfaces. Therefore, the heat exchange efficiency is remarkably improved between the first fluid such as warm water flowing through the insides of the flat tubes and the second fluid such as air flowing at the outsides.

Abstract: A heat exchanger has a plurality of oil core plates, and a plurality of coolant core plates, with each plate having an oil inlet opening adjacent one end of the plate, an oil outlet opening spaced from the oil inlet opening towards an opposed end of the plate, a coolant inlet opening, and a coolant outlet opening, and with the coolant inlet and outlet openings being adjacent the opposed end of the plate. Each oil core plate has an inwardly inclined, upstanding flange surrounding the oil inlet opening in the plate except for a portion thereof adjacent the one end of the plate at which a gap is provided in the flange. The oil outlet opening in the plate extends to adjacent the opposed end of the plate, and a further inwardly inclined, upstanding flange surrounds the oil outlet opening in the plate except adjacent the opposed end of the plate at which a further gap or gaps are provided in the further flange.

Abstract: A double sided-double heat exchanger core includes a plurality of sets of fluid passageways separated by a plurality of “S” shaped thermally conductive walls. Each set includes a plurality of fluid passageways. Each thermally conductive wall is configured to separate fluid flow between adjacent sets and configured to separate fluid flow between fluid passageways of one of the adjacent sets. The heat exchanger core is configured to provide segregated fluid flow between adjacent sets of fluid passageways. This heat exchanger core is particularly applicable for cooling equipment cabinets, wherein the air used to cool the equipment is recirculated through a plurality of sets and ambient air flows through interlaced sets to cool the recirculated air.