WO2007032891A2 - Echangeur de chaleur haute temperature peu couteux - Google Patents

Echangeur de chaleur haute temperature peu couteux Download PDF

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Publication number
WO2007032891A2
WO2007032891A2 PCT/US2006/033439 US2006033439W WO2007032891A2 WO 2007032891 A2 WO2007032891 A2 WO 2007032891A2 US 2006033439 W US2006033439 W US 2006033439W WO 2007032891 A2 WO2007032891 A2 WO 2007032891A2
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WO
WIPO (PCT)
Prior art keywords
monolith
heat exchanger
metal
piece
seams
Prior art date
Application number
PCT/US2006/033439
Other languages
English (en)
Other versions
WO2007032891A3 (fr
Inventor
William A. Whittenberger
Original Assignee
Catacel Corp.
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
Priority claimed from US11/225,771 external-priority patent/US7594326B2/en
Priority claimed from US11/225,763 external-priority patent/US7591301B2/en
Application filed by Catacel Corp. filed Critical Catacel Corp.
Priority to EP06802430.6A priority Critical patent/EP1937401A4/fr
Priority to CA002622780A priority patent/CA2622780A1/fr
Publication of WO2007032891A2 publication Critical patent/WO2007032891A2/fr
Publication of WO2007032891A3 publication Critical patent/WO2007032891A3/fr

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • 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
    • F28D9/0025—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 being formed by zig-zag bend plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/249—Plate-type reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04067—Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins
    • H01M8/04074—Heat exchange unit structures specially adapted for fuel cell
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2453—Plates arranged in parallel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2456—Geometry of the plates
    • B01J2219/2459—Corrugated plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts
    • B01J2219/2479—Catalysts coated on the surface of plates or inserts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2483—Construction materials of the plates
    • B01J2219/2485—Metals or alloys
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2491—Other constructional details
    • B01J2219/2492—Assembling means
    • B01J2219/2493—Means for assembling plates together, e.g. sealing means, screws, bolts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0215—Coating
    • B01J37/0225—Coating of metal substrates
    • 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
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0043—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for fuel cells
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells

Definitions

  • This invention relates to the field of heat exchange.
  • the invention provides a low-cost structure, capable of tolerating high operating temperatures, comprising a heat-exchanger or reactor such as is typically used in fuel processing or heat recovery for fuel cell systems.
  • heat exchangers are typically provided to recover waste heat from a hot exhaust stream, typically 500-1000° C, and to transfer the recovered heat to one of the inputs to the system, such as fuel, air, or steam.
  • heat exchangers that contain catalytic coatings are used as fuel processing reactors.
  • Each system may have a unique configuration, but virtually all such systems can be made more efficient by the appropriate use of heat exchangers.
  • there is a need for a low-cost heat exchanger that can tolerate the above-described high-temperature environment, and which can be provided in large quantities, so that heat exchangers can be installed at multiple locations within a facility, at a reasonable cost.
  • Such a heat exchanger has even more utility if one or more catalytic coatings can easily be applied to its working surfaces.
  • One way to limit the cost of a heat exchanger is to use a less expensive material in the manufacturing process.
  • the use of metal foil materials having a thickness in the range of about 0.001-0.010 inches, reduces expense by using less material overall.
  • foil materials are difficult to seal or weld using conventional processes.
  • Furnace brazing may be used to join certain high-temperature foil materials that contain nickel. Alloys that may be easily brazed include the 300 series stainless steel family (i.e. alloys known by the designations 304, 316, 321, etc.), the Inconel family (having designations 600, 601, 625, etc.), and other exotic alloys (Hastelloy-X and Haynes 230, for example).
  • brazable alloys are always expensive because they contain nickel. To limit the cost of material, it is highly desirable to use a high-temperature foil alloy that does not contain nickel.
  • Fecralloy which contains iron, chromium, and aluminum
  • Fecralloy is a now-cancelled trademark, formerly registered by the United Kingdom Atomic Energy Authority.
  • Fecralloy is quite inexpensive, relative to other high-temperature alloys, but it is difficult to braze. Because Fecralloy contains aluminum, the application of heat causes aluminum oxide to form, making it difficult to seal the structure by brazing.
  • the heat exchanger of the present invention provides a solution to the above-described problems, by providing a high-temperature heat exchanger that is both effective and inexpensive.
  • the present invention makes it economically feasible to place heat exchangers at multiple points in a fuel cell system.
  • the present invention could also be used in other industrial applications, such as in chemical plants.
  • the heat exchanger of the present invention may also be used in a steam reforming process, in which hydrocarbons are converted to hydrogen, for use in operating a fuel cell.
  • a steam reforming process is described in U.S. Patent Applications Serial No. 10/211,083, Serial No. 10/347,130, and Serial No. 10/888,488, the disclosures of which are incorporated by reference herein.
  • the above-cited applications show various uses of heat exchange, such as in conducting an endothermic steam reforming reaction on one side of a metal strip and an exothermic combustion reaction on the other side, or in conducting a water-gas shift reaction.
  • the operation of a fuel cell presents many situations in which heat from an exothermic reaction, or from a hot exhaust source, can be used to heat some other fluid stream.
  • the heat exchanger of the present invention is also compact, making it convenient for use in systems where a large amount of space is not available.
  • the heat exchanger of the present invention also has the advantage of being hermetically sealed, so that there is virtually no possibility of leakage.
  • One aspect of the present invention is an element, or building block, for a heat exchanger, comprising a monolith formed of a piece of metal that has been folded back and forth upon itself, and a comb inserted into folds of the monolith, at or near the end of the monolith.
  • the comb and the monolith are in contact along a plurality of seams, and these seams are hermetically sealed, preferably by laser welding.
  • the heat exchanger element can be used to form a complete heat exchanger.
  • the present invention comprises a complete heat exchanger formed of a monolith made of a piece of metal, preferably a metal foil.
  • the piece of metal foil has notches or cut-outs at opposite ends, and is folded back and forth upon itself to form the monolith, the notches or cut-outs defining openings which provide access to two distinct interior regions of the monolith.
  • a duct-defining means is affixed to both ends of the monolith, at locations corresponding to the openings.
  • the duct- defining means may include a comb having teeth which engage the folds of the monolith, a rectangular piece of metal, and a duct box which is inserted over the end of the monolith, the duct box including portions which, together with the rectangular piece and a spine of the comb, define a duct.
  • the duct may be made fluid-impervious by sealing its joints, such as by brazing or by welding, and preferably by laser welding.
  • the monolith defines two sides, corresponding to the two sides of the original piece of metal that is folded to form the monolith. These sides define distinct fluid flow regions within the monolith.
  • the two ducts, described above, provide fluid access to the two respective regions.
  • the metal defining the monolith is not coated with a catalyst, as such coating makes it difficult to weld or braze the structure.
  • the catalyst coating on the corrugated pieces inserted into one region of the monolith may be different from the coating on the pieces inserted into the other region.
  • two different reactions can be conducted separately, in the two distinct regions within the monolith.
  • the fluids flowing through the two ducts are not in direct fluid contact with each other, but are in heat exchange relationship, these fluids being separated by the folds of the monolith.
  • the invention also includes a method of making the above-described heat exchanger.
  • the method begins with cutting notches into a flat piece of metal, on opposite sides of the piece, and folding the piece of metal back and forth to form a monolith.
  • one attaches combs to the ends of the monolith, by inserting the teeth of the combs into the monolith, so as to engage the folds.
  • one affixes rectangular pieces of metal to the monolith, near the ends.
  • the duct boxes include metal portions which, together with spines of the combs and the rectangular pieces, define complete ducts which provide fluid communication with the respective distinct interior regions of the monolith.
  • a plurality of distinct corrugated pieces of metal are inserted into the spaces between folds of the monolith.
  • the corrugated pieces may be entirely or partly coated with a catalyst.
  • the ducts are preferably sealed by brazing or welding.
  • the present invention therefore has the primary object of providing a low-cost, high-temperature heat exchanger.
  • the invention has the further object of providing an element, or building block, for a low-cost, high-temperature heat exchanger.
  • the invention has the further object of providing a low-cost means of transferring heat in a fuel cell system or in an industrial plant.
  • the invention has the further object of providing a high-temperature heat exchanger which may be constructed of relatively inexpensive materials, using simple and economical construction techniques.
  • the invention has the further object of providing a low-cost, high- temperature heat exchanger which defines two distinct regions, wherein the heat exchanger can be used to conduct separate reactions in such regions.
  • the invention has the further object of providing a heat exchange structure which is easily coated with one or more catalytic materials to form a heat exchanging reactor.
  • the invention has the further object of making it economical to provide multiple heat exchangers at multiple locations in an industrial plant.
  • the invention has the further object of providing a method of making a low-cost, high-temperature heat exchanger.
  • the invention has the further object of providing a method of making an element, or building block, for a low-cost, high-temperature heat exchanger.
  • the invention has the further object of reducing the cost of providing heat exchange in a fuel cell system, or in an industrial plant.
  • Figure 1 provides a plan view of a piece of metal foil that has been prepared for fabrication into a heat exchanger of the present invention.
  • Figure 2 provides an end view of the foil of Figure 1, after the foil has been folded back and forth upon itself to define a monolith.
  • Figure 3 provides a perspective view of the folded foil of Figure 2.
  • Figure 4 provides a plan view of a comb which is used in making the heat exchanger of the present invention.
  • Figure 5 provides a plan view of a rectangular piece of metal, used in the manufacture of the heat exchanger of the present invention.
  • Figure 6a provides an elevational view of the folded foil monolith of Figure 3, and showing components forming ducts at each end.
  • Figure 6b provides an elevational view of the structure of Figure 6a, the monolith having been rotated by 90° relative to the structure of Figure 6a.
  • Figure 6c provides an end view of the monolith of Figure 6a.
  • Figure 7a provides an exploded perspective view showing a duct box before it has been installed over an end of the monolith forming the heat exchanger of the present invention.
  • Figure 7b provides a perspective view of the structures shown in Figure 7a, showing the duct box installed over the end of the monolith.
  • Figure 8a provides an elevational view of the structure shown in Figure 7b.
  • Figure 8b provides an elevational view of the structure of Figure 8a, the monolith having been rotated by 90° relative to the structure of Figure 8a.
  • Figure 8c provides an end view of the monolith of Figure 8a.
  • Figure 9 provides an end view of the heat exchanger of the present invention, including the cut pieces of corrugated foil inserted within folds of the monolith.
  • Figure 10 provides an exploded perspective view, showing the various components of the heat exchanger of the present invention.
  • Figure 11 provides a perspective view of a comb which has been inserted into the monolith of Figure 3, and showing the joints being sealed by a laser welder.
  • Figure 12 provides a perspective view of an alternative embodiment of the monolith, wherein a single cut is made in each corner of the original piece of metal, and wherein wings are folded from the monolith to define part of a duct.
  • Figure 13 provides a perspective view of another alternative embodiment, wherein the metal defining the monolith does not have notches or cuts, and wherein a separate piece of metal is used to cover the monolith and to define part of a duct.
  • the present invention comprises a heat exchanger which is constructed of relatively inexpensive, thin metal foil, rated for high temperatures, and in which the joints defined by the heat exchanger are sealed by laser welding. Laser welding makes it possible to use inexpensive, thin foil, while still providing a hermetically sealed structure.
  • the foil used in the present invention preferably has a thickness in the range of about 0.001-0.010 inches, and a more preferred range of about 0.002-0.005 inches.
  • the invention also includes an element, or building block, for a heat exchanger, comprising a monolith formed of a piece of metal that has been folded back and forth upon itself.
  • a comb is inserted into folds defined by the monolith, at or near an end of the monolith.
  • the comb and the monolith are in contact along a plurality of seams, and these seams are hermetically sealed, preferably by laser welding or by other means.
  • the heat exchanger element can be combined with other structures to form a complete heat exchanger, as will be described below.
  • a first embodiment of a completed low-cost heat exchanger of the present invention is manufactured in the following way. First, as shown in Figure 1, a flat, preferably rectangular, piece of metal foil 1 is prepared.
  • Notches or cut-outs 2 and 3 are formed at opposite corners of the foil.
  • the foil is to be folded back and forth upon itself, in a zigzag fashion, to form a monolith, the dashed lines indicating the locations of the folds.
  • End flaps 4 and 5 will serve as a shell for the monolith, as will be described later.
  • the thickness of the foil is preferably chosen to be less than about 0.008 inches, so as to minimize the cost.
  • the foil may be nickel -based, which is somewhat more expensive, or more preferably a lower-cost iron- based material such as that sold under the name Fecralloy.
  • Figures 2 and 3 illustrate the monolith 6 that is formed by folding the foil of Figure 1.
  • Figure 2 shows an end view
  • Figure 3 shows a perspective view.
  • Figures 2 and 3 clearly show the end flaps 4 and 5.
  • the shell, as described so far, is incomplete, insofar as the notches or cut-outs 2 and 3 of Figure 1 create openings which expose the interior regions of the monolith, as illustrated in Figure 3.
  • Figure 4 shows a comb 13 which is to be inserted at the end of the monolith.
  • Each monolith requires two combs, one at each end.
  • the comb serves the purposes of anchoring the folds of the monolith, and of defining part of a duct connected to the monolith.
  • the comb also holds the folds in spaced-apart relationship, facilitating the insertion of cut pieces of corrugated metal foil, as will be described later.
  • the comb includes teeth 10 and spine 11.
  • the spine later becomes a wall of the duct.
  • the comb is preferably made of a material having a greater thickness than that of the foil.
  • the comb could be made of stainless steel, or other high-temperature alloys, having a thickness in the range of about 0.03-0.06 inches.
  • the comb may be laser-cut from a sheet of metal, or it may be prepared in other ways.
  • Figure 5 illustrates a rectangular piece of metal 12 which is used to form the wall of the duct which is opposite the wall defined by spine 11 of the comb.
  • Each monolith requires two such rectangular pieces, one for each end.
  • the rectangular piece can be made of the same material, and having the same thickness, as the comb, or it can be made of thinner material. If the duct is to be welded to an external component, it is preferred that the rectangular piece be as thick as the spine of the comb. If the structure is to be brazed only, the rectangular piece could be of the same thickness as the body of the monolith, which is normally less than that of the spine of the comb.
  • Figures 6a-6c illustrate the next step in the manufacture of a heat exchanger according to the present invention.
  • Figure 6a shows an elevational view of the monolith, with the combs inserted at both ends, and showing rectangular pieces 12 attached. Each comb is inserted such that its teeth 10 fit between alternate folds of the folded foil. The comb therefore anchors the folds, holding them in the desired spaced-apart position.
  • Figure 6a clearly shows how the rectangular piece 12 and the spine 11 of the comb together define opposing walls of a duct.
  • the rectangular piece 12 is spaced from the end of the monolith by a distance which corresponds to the depth of the notches or cut-outs originally formed in the foil.
  • Figure 6b shows the same structure as Figure 6a, rotated by 90°.
  • Figure 6c shows an end view, as seen from the bottom portion of Figure 6a, illustrating the comb and also showing the rectangular piece 12 which is attached to the opposite end of the monolith.
  • FIGS 7a and 7b The next step in the manufacture of a heat exchanger of the present invention is illustrated in Figures 7a and 7b.
  • a duct box 15 is inserted over the ends of the monolith, as described below.
  • the duct box comprises a unitary structure having two contiguous parts, the first part defining a complete box with four walls, and the second part being open and having only three walls.
  • the first part has portions 18 and 19 which are bent over to join each other, thus forming a wall of the box, but the second part has portions 16 and 17 which are not folded over, and which leave the second part of the box without a corresponding wall.
  • the dimensions of the box are chosen such that the second part can snugly fit over the end of the monolith.
  • Figure 7b illustrates the structure where the box has been fully inserted over the end of the monolith. Note that in Figure 7b, the portions 16 and 17, together with the spine 11 of the comb and the rectangular piece 12, form a complete duct for providing fluid communication with an interior region of the monolith.
  • Figures 8a-8c provide elevational and end views of the structure described with respect to Figures 7a and 7b.
  • Figure 8a shows duct boxes 15 installed at both ends of the monolith.
  • Figure 8b shows an elevation that is rotated by 90° relative to Figure 8a.
  • Figure 8b therefore provides a view as seen when looking into the duct, and shows the exposed interior of the monolith.
  • Figure 8c provides an end view, as seen from the bottom of the structure of Figure 8a.
  • Figure 9 provides an end view of the monolith, showing a plurality of cut pieces of corrugated foil 21 inserted within the spaces defined by the folded foil.
  • the insertion of cut pieces 21 is performed after the foil 1 has been folded into a monolith, and preferably after the combs, rectangular pieces, and duct boxes have been installed.
  • the comb serves to facilitate the insertion of the cut pieces of corrugated foil, as it maintains the spacing between adjacent folds of the foil 1.
  • Figure 9 clearly shows the teeth 10 of the comb, inserted into the folds of the monolith. Note that half of the cut pieces must be inserted at one end, and the other half must be inserted from the other end. The reason for the latter is that the teeth of the comb block half of the channels. The channels blocked at one end are not blocked at the other end.
  • the cut pieces 21 can be inserted manually, one piece at a time. Alternatively, the cut pieces can be stacked in a magazine which holds them in the correct position, and the pieces can then be pushed simultaneously into the monolith.
  • the cut pieces 21 may be coated with a suitable combustion catalyst, or other catalyst, depending on the intended use of the heat exchanger.
  • the cut pieces may be wholly or partially coated.
  • the metal foil defining the monolith is normally not coated, as a coating would make it difficult to weld or braze. But if it were desired to coat the monolith, such coating could be done by dip coating the assembled structure.
  • Figure 10 provides an exploded perspective view which summarizes the construction of the heat exchanger of the present invention.
  • the foil 1 is shown, after having been folded into a monolith, leaving openings for the ducts, defined by the notches or cut-outs described above.
  • the figure clearly shows the monolith shell, defined by the flaps in the original piece of metal foil described above, and by the first and last folds of the monolith.
  • the comb 13 is to be affixed to the end of the monolith, to hold the folds in spaced-apart relation, and to define a wall of the duct.
  • the rectangular piece 12 is similarly attached to the monolith, to define the opposite wall of the duct.
  • the cut pieces 21 of corrugated foil are inserted into the spaces between adjacent folds.
  • the foil used to make the cut pieces 21 can be very low-cost corrugated foil, which could be made of Fecralloy, having a thickness of the order of about 0.002 inches.
  • the cut pieces 21 are shown to define straight channels, but one could instead use a variety of channel configurations, such as wavy or skew corrugations, as are known in the heat exchange industry, to promote heat transfer.
  • the cut pieces can be coated on one side or both sides. As noted above, each side could be wholly or partly coated. Because both sides of a given cut piece will belong to the same fluid flow region of the monolith, it is preferred that, if a catalyst coating is used, the same catalyst should be used on both sides. But the invention is not limited to this configuration, and it is conceivable that different catalysts could be coated onto the two sides of the cut pieces.
  • the folded structure of the monolith inherently defines two sides, each side corresponding to a respective side of the original piece of metal foil.
  • the monolith therefore defines two distinct fluid flow regions, corresponding to the two sides of the original piece. These two regions are not in direct fluid communication with each other, but are in heat exchange relationship, as heat can flow through the foil which separates the regions from each other.
  • the two ducts provide access to the two respective fluid flow regions of the monolith. It is clear, therefore, that by placing a first catalyst on the cut pieces belonging to the first region, and a second catalyst on the cut pieces belonging to the second region, one can conduct two distinct reactions in the two regions of the monolith.
  • a process for making the low-cost heat exchanger of the present invention can be summarized as follows. First, one prepares the flat foil, with notches or cut-outs at the corners, and folds the foil back and forth upon itself to form the monolith. Next, one forms the combs, such as by laser cutting, and inserts a comb into each end of the monolith. Next, one forms a duct box for each end, and a rectangular piece, and one affixes the rectangular piece to the monolith, and one slides the duct boxes onto the ends. Next, one applies a brazing alloy to all joints on the resulting structure, and brazes the structure in a suitable furnace. Finally, one inserts the cut pieces of corrugated foil, which may or may not have a catalyst coating, into the spaces defined by the monolith.
  • the foil must be a nickel -based alloy.
  • a 300 series stainless steel alloy which is of medium expense, is preferred.
  • the foil is preferably a relatively expensive nickel -based alloy, typically the alloy sold under the trademark Inconel .
  • a preferred alternative, for all temperature ranges, is to use a relatively inexpensive iron-based foil, such as that sold under the name Fecralloy. In the latter case, before the duct boxes are installed, one would weld the joints where the foil defining the monolith meets the combs, preferably by laser welding. After installation of the duct boxes, the brazing alloy would be applied to the duct joints, not to all joints.
  • the invention can be practiced with yet another process which avoids brazing altogether.
  • one forms the duct boxes and rectangles, and installs them as described above.
  • FIG 11 shows the use of a laser welding device for sealing the heat exchanger of the present invention.
  • metal foil 1 has been folded into a monolith, and comb 13 has been inserted at one end.
  • a laser welding machine includes computer-controlled device 26 which is programmed to control the orientation and power level of laser head 25.
  • the device 26 is preferably capable of precisely positioning the laser beam with a multiple-axis control.
  • a laser beam 23 is traced across all of the seams where the monolith meets the teeth of the comb. Heat from the laser beam causes the metal to soften or melt locally, and to form a fusion weld between the comb and the foil defining the monolith.
  • the precise positioning of the laser beam enables the weld to be formed at all locations where the comb and the monolith meet. The result is a strong mechanical joint which also comprises a gas-tight seal.
  • the structure of the heat exchanger as described above, can be varied, as described below.
  • Figure 12 One alternative embodiment is illustrated in Figure 12. Unlike the previous embodiment in which rectangular notches were formed by making two cuts at opposite corners of the flat metal foil, the embodiment of Figure 12 uses only a single cut at such corners. The cut allows the formation of flaps 27 and 28, which are folded along a line which would have been the location of the other cut in the previous embodiment. The flaps 27 and 28 are positioned such they perform the function of the rectangular pieces 12 of the previous embodiment. The embodiment of Figure 12 reduces the number of seams to be sealed, because the flaps 27 and 28 are integrally formed with the monolith.
  • Figure 13 shows another alternative embodiment.
  • no notches or cuts are made in the foil defining the monolith 6.
  • separate side cover pieces 30 are made for each side of the monolith.
  • the cover pieces are made from foil, which may be the same as that used to make the monolith, or which may be made of thicker material.
  • the cover piece includes a side panel 31 and a flap 32. The side panel is joined to the monolith, preferably by welding, and the flap 32 performs the function of rectangular piece 12 of the first embodiment.
  • Figures 12 and 13 do not show the duct boxes or the cut corrugated pieces. It is understood that such components, as described with respect to the previous embodiments, would be included in the complete heat exchanger.
  • the invention can be modified in other ways, which will be apparent to the reader skilled in the art.
  • the construction of the ducts, at or near the ends of the monolith can be accomplished in different ways.
  • the duct boxes, combs, and rectangular pieces comprise means for defining the ducts.
  • the components could be varied, as long as the ducts are constructed to convey fluid, sealed from the outside, into or out of the appropriate portion of the monolith.
  • the order of the steps of the assembly of the heat exchanger can be varied somewhat. For example, it is not necessary to prepare the combs 13 before the rectangular pieces 12; instead, the order of these two steps could be reversed.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

L'invention concerne un échangeur de chaleur haute température peu coûteux fait d'une pièce métallique découpée, le métal étant ensuite replié sur lui-même en accordéon pour former un monolithe. Les découpages dans la pièce métallique forment des ouvertures qui communiquent avec des faces distinctes du monolithe. Des tuyaux sont fixés aux ouvertures. Des pièces découpées de métal ondulé, qui peuvent comporter un revêtement catalyseur, sont insérées entre des plis du monolithe. L'échangeur de chaleur peut faire partie d'un système de piles à combustible, ou être utilisé dans d'autres applications industrielles pour récupérer la chaleur résiduelle ou mettre en oeuvre diverses réactions catalytiques et non catalytiques. L'invention comprend également un élément, ou unité élémentaire, pour échangeur de chaleur haute température, qui comprend un monolithe de métal replié dans lequel sont insérés des peignes métalliques, le monolithe et les peignes définissant des jonctions hermétiquement étanches.
PCT/US2006/033439 2005-09-13 2006-08-28 Echangeur de chaleur haute temperature peu couteux WO2007032891A2 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP06802430.6A EP1937401A4 (fr) 2005-09-13 2006-08-28 Echangeur de chaleur haute temperature peu couteux
CA002622780A CA2622780A1 (fr) 2005-09-13 2006-08-28 Echangeur de chaleur haute temperature peu couteux

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US11/225,771 2005-09-13
US11/225,763 2005-09-13
US11/225,771 US7594326B2 (en) 2005-09-13 2005-09-13 Method for making a low-cost high-temperature heat exchanger
US11/225,763 US7591301B2 (en) 2005-09-13 2005-09-13 Low-cost high-temperature heat exchanger

Publications (2)

Publication Number Publication Date
WO2007032891A2 true WO2007032891A2 (fr) 2007-03-22
WO2007032891A3 WO2007032891A3 (fr) 2009-06-11

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EP2015866A2 (fr) * 2006-05-08 2009-01-21 CompactGTL plc Structure de catalyseur pour reaction rapide
US10557670B2 (en) 2014-05-30 2020-02-11 Pleat As Device for heat exchange

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JP2003185365A (ja) * 2001-12-25 2003-07-03 Furukawa Electric Co Ltd:The 熱交換器
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US3734177A (en) * 1972-02-04 1973-05-22 Modine Mfg Co Heat exchanger
JPS55118598A (en) * 1979-03-06 1980-09-11 Braun Kk Heat exchanger
US7159649B2 (en) * 2004-03-11 2007-01-09 Thermal Corp. Air-to-air heat exchanger

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2015866A2 (fr) * 2006-05-08 2009-01-21 CompactGTL plc Structure de catalyseur pour reaction rapide
EP2015866B1 (fr) * 2006-05-08 2011-09-14 CompactGTL plc Reacteur catalytique comprenant premier et second catalysateur
US10557670B2 (en) 2014-05-30 2020-02-11 Pleat As Device for heat exchange

Also Published As

Publication number Publication date
EP1937401A4 (fr) 2013-06-19
WO2007032891A3 (fr) 2009-06-11
EP1937401A2 (fr) 2008-07-02
CA2622780A1 (fr) 2007-03-22

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