AU755650B2 - Hydrogen generators - Google Patents
Hydrogen generators Download PDFInfo
- Publication number
- AU755650B2 AU755650B2 AU81258/98A AU8125898A AU755650B2 AU 755650 B2 AU755650 B2 AU 755650B2 AU 81258/98 A AU81258/98 A AU 81258/98A AU 8125898 A AU8125898 A AU 8125898A AU 755650 B2 AU755650 B2 AU 755650B2
- Authority
- AU
- Australia
- Prior art keywords
- copper
- frame
- membrane
- hydrogen
- diffusion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
- 239000001257 hydrogen Substances 0.000 title claims description 32
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 32
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 25
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 49
- 239000010949 copper Substances 0.000 claims description 45
- 229910052802 copper Inorganic materials 0.000 claims description 44
- 239000012528 membrane Substances 0.000 claims description 29
- 238000000034 method Methods 0.000 claims description 13
- 238000000576 coating method Methods 0.000 claims description 9
- 239000011248 coating agent Substances 0.000 claims description 8
- 150000002431 hydrogen Chemical class 0.000 claims description 8
- 230000002093 peripheral effect Effects 0.000 claims description 7
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 4
- 239000010962 carbon steel Substances 0.000 claims description 4
- 238000007747 plating Methods 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 2
- 238000005498 polishing Methods 0.000 claims 1
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical group [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 28
- 239000011888 foil Substances 0.000 description 12
- 229910052751 metal Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 238000009792 diffusion process Methods 0.000 description 8
- 230000000712 assembly Effects 0.000 description 7
- 238000000429 assembly Methods 0.000 description 7
- 238000003466 welding Methods 0.000 description 7
- 229910000881 Cu alloy Inorganic materials 0.000 description 5
- 229910045601 alloy Inorganic materials 0.000 description 5
- 239000000956 alloy Substances 0.000 description 5
- 239000001307 helium Substances 0.000 description 4
- 229910052734 helium Inorganic materials 0.000 description 4
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 4
- 229910052763 palladium Inorganic materials 0.000 description 4
- 230000004907 flux Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 229910001252 Pd alloy Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000001996 bearing alloy Substances 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000004320 controlled atmosphere Methods 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000013023 gasketing Methods 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 229910000765 intermetallic Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0039—Inorganic membrane manufacture
- B01D67/0069—Inorganic membrane manufacture by deposition from the liquid phase, e.g. electrochemical deposition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D53/228—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
- B01D71/022—Metals
- B01D71/0227—Metals comprising an intermediate layer for avoiding intermetallic diffusion
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
- C01B3/501—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion
- C01B3/503—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion characterised by the membrane
- C01B3/505—Membranes containing palladium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/108—Hydrogen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/08—Specific temperatures applied
- B01D2323/081—Heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2323/00—Details relating to membrane preparation
- B01D2323/12—Specific ratios of components used
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S55/00—Gas separation
- Y10S55/05—Methods of making filter
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Electrochemistry (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Hydrogen, Water And Hydrids (AREA)
Description
HYDROGEN GENERATORS FIELD OF THE INVENTION This invention relates to hydrogen-selective membrane walls for connecting the high pressure chamber to the low pressure chamber of apparatus for the preparation of pure hydrogen at elevated temperatures.
BACKGROUND OF THE INVENTION The discussion of the background to the invention herein is included to explain the context of the invention. This is not to be taken as an admission that any of the material referred to was published, known or part of the common general knowledge in Australia as at the priority date of any of the claims.
0: *:.The prior art is replete with descriptions of palladium-bearing alloy membranes used to prepare pure hydrogen from gaseous hydrogen-containing mixtures by o permeation through a palladium bearing metallic membrane under pressure and at 0 elevated temperatures. Reference is made to the co-pending patent application .OgO Serial No. 08/719,385 of common assignee which is incorporated herein by reference, wherein an important advantage of a 60% palladium-40% copper alloy 20 membrane with respect to temperature-cycling and minimal swelling in hydrogen is disclosed. This bears also on the publication by J. Shu, B.P. Grandjean, A. van Neste and S. Kaliaguine, entitled "Catalytic Palladium based Membrane Reactors: A Review", The Canadian Journal of Chemical Engineering, Vol. 69, (October, 1991) herein also incorporated by reference, wherein this particular palladium-copper alloy is described as showing a sharp maximum at 40 wt% Cu.
Accordingly, for the purpose of the present invention, we use such palladium copper alloys with copper contents sufficiently near the 40% by weight optimum, (i.e.
36-42% Cu), in which narrow range more than two thirds of the maximum flux is retained. Such alloys are termed "Pd/40% Cu" in this specification and the appended claims.
1258-98Adoc WO 00/05169 PCT/IB98/01120 2 As shown, for example, in the above reference co-pending application, Pd alloy membranes can be in the firm of thin flat foils or small diameter tubes 2mm Foils of the Cu membrane are readily available in thicknesses of 0.001 to 0.0025 inches, whereas special expensive techniques are required to make such Pd/40% Cu tubes with wall thicknesses of no less than 0.0025 inch.
As also disclosed in the above-referenced co-pending application, a palladium alloy foil can be sandwiched between gaskets, and the edge area of the sandwich can be pressed onto a metallic frame. To so produce a leak-tight two-chamber apparatus, a uniform weighty and costly edge pressure is required to at least balance the pressure in the high pressure chamber. It is thus importance to replace, in a pure hydrogen generator, the gasket seal with a pressure-tight seal, such as a weld. Welding is preferred over brazing or soldering to avoid contamination of the foil by the extraneous metals of the latter.
Diffusion welding employs temperatures that range from 50 to 75% of the melting point ["Procedure Development and Practice Considerations for Diffusion Welding", by S.B.
Dunkerton, "ASM Handbook", vol. 6, p. 883, ASM International (1993)]. Diffusion welding of copper to a different metal or to an alloy "is conducted at a temperature greater than onehalf of the absolute melting point" [Diffusion welding of Solid-State Welding, by J.L. Jollison and F.J. Zanner, "Metals Handbook", 9th Ed. Vol. 6, p. 672, ASM International (1988); see first column on page 672 and Table 1 on page 677].
The Pd/40% Cu alloy has a melting point of approximately 1200 0 C (1473 K) ["ASM Handbook", vol. 3, p. 717, ASM International (1993)]. Hence welding it to copper is expected to require'a temperature in excess of about 460 0 C (733 However, we have found that the hydrogen flux across the Pd/40% Cu foil deteriorates after the foil has been exposed to such high temperatures.
SUBSTITUTE SHEET (R ULE 26) 3 Underlying the present invention is the discovery that these problems can be overcome by providing a hydrogen selective Pd/40% Cu membrane wall in the form of a thin palladium-copper alloy membrane of carefully controlled composition in an open-area copper surfaced metallic frame, bonded, preferably hermetically bonded, by diffusion-bonding the membrane to the frame.
The term "diffusion-bonding", as used herein means controlling and maintaining an elevated bonding temperature below about 350 0 C, while subjecting the edge area of the membrane in contact with the frame to a substantially uniform high pressure, 10 in an oxygen-free atmosphere.
"OBJECTS AND ADVANTAGES OF THE INVENTION It is an object of the invention to provide a high pressure-low pressure chamber apparatus for the permeation of pure hydrogen across a hydrogen selective membrane which overcomes, or at least alleviates, one or more disadvantages of the prior art.
It is a further object to provide a method of producing a Pd/40% Cu foil membrane bonded to a copper surfaced metallic frame which overcomes or at least alleviates, i 20 one or more disadvantages of the prior art.
An advantage of this invention is the provision of a novel, much lower-temperature, diffusion-bonding technique of Pd/40% Cu to copper which avoid flux deterioration, as well as the need for excessive edge gasket compression.
Another advantage of this invention is the provision of a new and improved pure hydrogen-permeating membrane wall having a Pd/40% Cu foil bonded, preferably hermetically bonded, by such technique to a copper surface on a temperature and pressure-resistant, herein termed "firm", metal frame.
Other and further objects and advantages will be explained hereinafter and are more fully delineated in the appended claims.
SUMMARY OF THE INVENTION According to the present invention, there is provided an assembly including a thin Cu foil having its peripheral region diffusion-bonded to a copper-surfaced metallic frame.
The present invention also provides a high pressure-low pressure chamber apparatus for the permeation, under a pressure differential, of pure hydrogen across a hydrogen-selective membrane at an elevated temperature and having a wall connecting the high-pressure chamber to the low pressure chamber, said wall 10 including a thin Pd/40% Cu foil membrane having its edge hermetically diffusion- .bonded to a copper surfaced metallic frame.
The present invention further provides a method of producing a Pd/40% Cu foil membrane bonded to a copper-surfaced metallic frame that includes exposing said frame and membrane to hydrogen, contacting the peripheral region of said membrane with said copper frame and applying to said peripheral region, at a controlled elevated temperature between 2000 and 350°C, a substantially uniform high pressure thereby diffusion-bonding said membrane to the copper surface of said frame.
1258-98A.doc claims means a copper coating as well as a copper-rich alloy coating of sufficient copper content for diffusion-bonding.
The novel diffusion-bonding technique of this invention comprises the step of pressing a thin Pd/40% Cu foil, preferably 0.001-0.0025 inches thick, onto a coppersurfaced frame, after exposure to or, preferably in a hydrogen-containing atmosphere, in the range of 2000 to 3500 and more particularly between 2900 and 3250, for example, for a cycle period of several hours in a hydrogen atmosphere furnace.
The novel wall of this invention comprises a polished firm metallic frame made of carbon steel or stainless steels or others, an adherent, preferably electroplated, e copper surface thereon, and a thin Pd/40% Cu membrane foil having its peripheral region preferably hermetically sealed to the copper surface by the above diffusion- Is bonding technique.
Preferred and best made designs and techniques are later presented.
DESCRIPTION OF THE DRAWING lille= S The invention will now be described in connection with the accompanying drawing, the single figure of which is a schematic top view of a metal frame having its open area covered by a Pd/40% Cu foil with the foil edge area diffusion-bonded to the frame, in accordance with the invention.
DESCRIPTION OF PREFERRED EMBODIMENTS We propose, as above stated, to take advantage of the availability and of the low cost (relative to tubes) of a thin Pd/40% Cu foil membrane by diffusion-bonding it hermetically to W:\may\MMNMfDEL\825S-98A do WO 00/05169 PCT/IB98/01120 a frame to form a wall which, in a pure hydrogen generator, obviates gasketing and the excessive mechanical pressure required therefor.
Surprisingly, we have found that a Pd/40% Cu foil can be diffusion-bonded to copper under pressure and, after exposure to and, preferably in the presence of hydrogen, even when the temperature is in the low range of 2000 to 350 0 C, and preferably between 2900 and 325°C.
While we do not wish to be held to any theory, it is believable that the bond results, at least in part, from copper inter-metallic diffusion and that the hydrogen exposure eliminates any interfering oxide layer.
This mode of diffusion bonding has been found not to be deleterious to the membrane, as evidenced by its durability, at the very same temperatures, when pure hydrogen is generated from a methanol-steam reformate, as described in the above-referred to copending patent application.
By way of example, referring now to the figure of the drawing, samples of Alloy 101 (i.e.
oxygen free) copper frames 1, each 1.5 inches square and 0.03125 inch thick, were center punched each with a 0.625 inch diameter hole. Pd/40% Cu foils, 3, each 0.001 inch thick and 1 inch diameter, were centered over the 0.625 inch diameter holes of the frames 1. The 0.1875 inch overlap edge perimeters 2 of each of the coils 3 were mechanically held under pressure by a pair of opposing flanges (not shown). The pressure was controlled by the torque load on the four flange bolts (also not shown).
After evenly tightening the flange bolts, the assemblies were loaded into a controlled atmosphere furnace for heat-treating. The furnace temperatures were varied between 2000 and 350°C with a slow flow of pure hydrogen gas through the furnace, which was held at atmosphere pressure, or alternatively under reduced pressure, for about twelve hours.
SUBSTITUTE SHEET (RULE 26) WO 00/05169 PCT/IB98/01120 6 The hermetic seals between the foils and the frames produced by the diffusion bonds were tested by subjecting the finished assemblies in a separate apparatus (also not shown) to a pressure gradient of helium gas of up to 150 psi for several hours. No gas leakage was observed.
When selecting a temperature range between 1900 and 3250C and flowing hydrogen at about atmospheric or reduced pressure, a mechanical perimeter pressure in the order of 5000 psi or more resulted in producing hermetic seals between the frame and the foil.
Bonding periods in the furnace vary with operating conditions. The required times for hermetic sealing are readily determined experimentally by selecting and controlling the temperature, edge pressure and either the pre-hydrogen exposure at an elevated temperature and/or the hydrogen atmosphere in the furnace, and then leak-testing the resultant assembly.
As the wall separating the high and low pressure chambers of a pure hydrogen generator, the diffusion-bonded assemblies of this invention must withstand the pressure differential at the elevated operating temperature. The above-described, 100% copper framed, diffusionbonded assemblies deformed badly under gas pressure above about 2000C. However, operation of such diffusion bonded assemblies below about 2000C is undesirable due to poor hydrogen permeability.
Hence for the purposes of this invention, we use a structurally firm frame made of a metal or an alloy subject to copper coating, which is not weakened under the operating temperatures and pressures of a pure hydrogen generator, such as carbon steel, stainless steel, or others, which, when not subject to copper coating, do not lend themselves to diffusion-bonding.
SUBSTITUTE SHEET (RULE 26) WO 00/05169 PCT/IB98/01120 7 We have found that diffusion-bonding, as herein described, of a Pd/40% Cu foil to a coppercoating plated onto such a firm metallic frame, results in an assembly, in which, surprisingly, the bond of the copper coating to the frame metal and the bond of the Pd/40% Cu foil to the copper coating, are both strong.
But, in leak tests of these assemblies, helium leaks were sometimes encountered. Though again we do not wish to be held to any theory, we have found it plausible to attribute the helium leaks either to the grainy streaks of the somewhat uneven surface of the metal frame, (which streaks were actually showing through the foil's edge area of the finished assembly) and/or to too thin a copper plate (such as less than 0.0005 inch thick).
Thus, to obtain consistent hermetic seals for the use of the assemblies in two-chamber hydrogen generators, we select thicker copper coatings and/or we polish the frame metal to provide a smooth even area prior to plating copper and diffusion-bonding Pd/40% Cu thereon. Those samples were leak proof in the helium leak test.
As a specific example of producing such a leak proof assembly, samples of a commercial grade "oil hardening" pre-ground flat stock carbon steel were prepared in the abovedescribed dimensions. Prior to copper plating, they were polished to a smooth finish, some by hand and others by electropolishing, cleaned by degreasing and picked. Some samples were also subjected to a short electrolytic "nickel strike" to assure good copper adhesion.
The samples were then electroplated from standard, e.g. cyanide or sulfate, baths to copper coating thicknesses of about 0.0005 to 0.0008 inch.
Diffusion-bonding of 0.001 inch thick Pd/40% Cu foils to the copper plated frames was then performed as above described.
SUBSTITUTE SHEET (RULE 26) WO 00/05169 PCT/IB98/01120 8 While preferred embodiments of the invention have been described in the foregoing, it will be apparent to those skilled in the art that they can be varied without departing from the scope of the invention.
SUBSTITUTE SHEET (RULE 26)
Claims (9)
1. An assembly including a thin Pd/40% Cu foil having its peripheral region diffusion-bonded to a copper-surfaced metallic frame.
2. A high npresure-lw pressure chamber appratus for the nprmeation, under a pressure differential, of pure hydrogen across a hydrogen-selective membrane at an elevated temperature and having a wall connecting the high- pressure chamber to the low pressure chamber, said wall including a thin Cu foil membrane having its edge hermetically diffusion-bonded to a copper surfaced metallic frame.
3. A high pressure-low pressure chamber apparatus as claimed in claim 2, wherein said metallic frame is one of polished carbon steel and stainless steel.
4. A high pressure-low pressure chamber apparatus as claimed in claims 2 or 3, wherein the copper surface frame is polished. *oo S *ooo
5. A method of producing a Pd/40% Cu foil membrane bonded to a copper- 20 surfaced metallic frame that includes exposing said frame and membrane to hydrogen, contacting the peripheral region of said membrane with said copper frame and applying to said peripheral region, at a controlled elevated temperature between 2000 and 350°C, a substantially uniform high pressure thereby diffusion- bonding said membrane to the copper surface of said frame.
6. A method as claimed in claim 5, wherein the hydrogen exposure and pressure application are carried out simultaneously.
7. A method as claimed in claims 5 or 6 including the prior steps of polishing said frame and plating a copper-coating thereon.
8. An assembly of claim 1, substantially as herein described with reference to -the accompanying drawings. W:\nary\MMHNODEL\81258-98A.doc
9. An apparatus of claim 2, substantially as herein described with reference to the accompanying drawings. A method of claim 5, substantially as herein described with reference to the accompanying drawings. DATED: 29 November 2001 PHILLIPS ORMONDE FITZPATRICK Patent Attorneys for: WALTER JUDA, CHARLES W. KRUEGER and R. TODD BOMBARD S oo @00. 0 o oo• kV %INII INODEL.8'i S-98.doc
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/IB1998/001120 WO2000005169A1 (en) | 1997-06-20 | 1998-07-23 | Hydrogen generators |
Publications (2)
Publication Number | Publication Date |
---|---|
AU8125898A AU8125898A (en) | 2000-02-14 |
AU755650B2 true AU755650B2 (en) | 2002-12-19 |
Family
ID=11004731
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU81258/98A Ceased AU755650B2 (en) | 1998-07-23 | 1998-07-23 | Hydrogen generators |
Country Status (5)
Country | Link |
---|---|
JP (1) | JP3955436B2 (en) |
AU (1) | AU755650B2 (en) |
CA (1) | CA2337123A1 (en) |
DE (1) | DE69824452T2 (en) |
HK (1) | HK1034950A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4490383B2 (en) * | 2006-03-13 | 2010-06-23 | 日本碍子株式会社 | Hydrogen gas separator fixing structure and hydrogen gas separator using the same |
JP4792598B2 (en) | 2008-03-24 | 2011-10-12 | 株式会社日本製鋼所 | Hydrogen permeation module and method of use thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0783919A1 (en) * | 1996-01-11 | 1997-07-16 | Bend Research, Inc. | Composite hydrogen separation element and module |
EP0796647A1 (en) * | 1996-03-18 | 1997-09-24 | Mitsubishi Jukogyo Kabushiki Kaisha | Hydrogen separation member |
-
1998
- 1998-07-23 CA CA002337123A patent/CA2337123A1/en not_active Abandoned
- 1998-07-23 DE DE69824452T patent/DE69824452T2/en not_active Expired - Fee Related
- 1998-07-23 JP JP2000561127A patent/JP3955436B2/en not_active Expired - Fee Related
- 1998-07-23 AU AU81258/98A patent/AU755650B2/en not_active Ceased
-
2001
- 2001-08-13 HK HK01105641A patent/HK1034950A1/en not_active IP Right Cessation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0783919A1 (en) * | 1996-01-11 | 1997-07-16 | Bend Research, Inc. | Composite hydrogen separation element and module |
EP0796647A1 (en) * | 1996-03-18 | 1997-09-24 | Mitsubishi Jukogyo Kabushiki Kaisha | Hydrogen separation member |
Also Published As
Publication number | Publication date |
---|---|
AU8125898A (en) | 2000-02-14 |
DE69824452D1 (en) | 2004-07-15 |
JP3955436B2 (en) | 2007-08-08 |
HK1034950A1 (en) | 2001-11-09 |
CA2337123A1 (en) | 2000-02-03 |
JP2002521180A (en) | 2002-07-16 |
DE69824452T2 (en) | 2005-06-23 |
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