CA2337123A1 - Hydrogen generators - Google Patents
Hydrogen generators Download PDFInfo
- Publication number
- CA2337123A1 CA2337123A1 CA002337123A CA2337123A CA2337123A1 CA 2337123 A1 CA2337123 A1 CA 2337123A1 CA 002337123 A CA002337123 A CA 002337123A CA 2337123 A CA2337123 A CA 2337123A CA 2337123 A1 CA2337123 A1 CA 2337123A1
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- CA
- Canada
- 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.)
- Abandoned
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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
-
- 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
-
- 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)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Analytical Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
A hydrogen-selective thin Pd/40 % Cu membrane for use as a wall connecting high and low pressure chambers of a hydrogen generator, wherein the membrane has its edge area diffusion bonded to a copper-surfaced metallic frame; and a method of preparing the same.
Description
HY~RpGEN GENERATORS
FIELD OF THE INVENTION
This invention relates to hydragen-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
to The prior art is replete with descriptions of palladium-bearing alloy membranes used to prepare pure hydrogen from gaseous hydrogen-containing mixtures by permeation through a palladium bearing metallic membrane under pressure and at elevated temperatures.
Reference is made to the co-pending patent application Serial No. 08/719,385 of common ~s assignee which is incorporated herein by reference, wherein an important advantage of a 60% palladium-40% copper alloy 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 Jouma! of Chemical Engineering, Vol. 69, (October, ~~0 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 ~~5 narrow range more than two thirds of the maximum flux is retained. Such alloys are termed "Pd/10% Cu" in this specification and the appended claims.
SUBSTI?'UTE SHEET (R ULE 26)
FIELD OF THE INVENTION
This invention relates to hydragen-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
to The prior art is replete with descriptions of palladium-bearing alloy membranes used to prepare pure hydrogen from gaseous hydrogen-containing mixtures by permeation through a palladium bearing metallic membrane under pressure and at elevated temperatures.
Reference is made to the co-pending patent application Serial No. 08/719,385 of common ~s assignee which is incorporated herein by reference, wherein an important advantage of a 60% palladium-40% copper alloy 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 Jouma! of Chemical Engineering, Vol. 69, (October, ~~0 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 ~~5 narrow range more than two thirds of the maximum flux is retained. Such alloys are termed "Pd/10% Cu" in this specification and the appended claims.
SUBSTI?'UTE SHEET (R ULE 26)
2 As shown, for example, in the above reference co-pending application, Pd alloy membranes can be in the firm of thin flat lfoils or small diameter tubes (e.g. 2mm O.D.). Foils of the Pd/40% 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 ~o 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.
t5 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 lntemational (1993)]. Diffusion welding of copper to a different metal or to an alloy "is conducted at a temperature greater than one-half of the absolute melting point" [Diffusion welding of Solid-State Welding, by J.L. Jollison 2o and F.J. Zanner, "Metals Handbook", 9'" 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°C (1473 K) ["ASM
Handbook", vol. 3, p. 717, ASM International (1993)]. Hence welding it to copper is 25 expected to require' a temperature in excess of about 460°C (733 K).
However, we have found that the hydrogen flux across the Pd/40% Cu foil deteriorates after the foil has been exposed to such high temperai:ures.
SUBSTITUTE SHEET' (RULE 26) to
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 ~o 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.
t5 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 lntemational (1993)]. Diffusion welding of copper to a different metal or to an alloy "is conducted at a temperature greater than one-half of the absolute melting point" [Diffusion welding of Solid-State Welding, by J.L. Jollison 2o and F.J. Zanner, "Metals Handbook", 9'" 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°C (1473 K) ["ASM
Handbook", vol. 3, p. 717, ASM International (1993)]. Hence welding it to copper is 25 expected to require' a temperature in excess of about 460°C (733 K).
However, we have found that the hydrogen flux across the Pd/40% Cu foil deteriorates after the foil has been exposed to such high temperai:ures.
SUBSTITUTE SHEET' (RULE 26) to
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, 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°C, while subjecting the edge area of the membrane in contact with the frame to a substantially uniform high pressure, in an oxygen-free atmosphere.
OBJECTS OF THE INVENTION
One object of this invention is to provide a novel, much lower temperature, diffusian-bonding technique of Pd/40% Cu to copper which avoids flux deterioration, as well as the need for t5 excessive edge gasket compression.
Another object of this invention is a new and improved pure hydrogen-permeating :?o :?5 membrane wall having a Pd/40°'o Cu foil hermetically bonded by such technique to a copper surface on a temperature and pressure-resistant, herein termed "firm", metal frame.
Other and further objects will be; explained hereinafter and are more fully delineated in the appended claims.
SUMMARY OF THE INVENTIOPJ
In summary, from one of its viewpoints, this invention broadly embraces an assembly comprising a thin Pd/40% Cu foill having its edge area diffusion-bonded to a copper-surfaced metallic frame. The term "copper surface" as used in this specification and in the appended SUBSTITUTE SHEET (RULE 26)
The term "diffusion-bonding", as used herein means controlling and maintaining an elevated bonding temperature below about 350°C, while subjecting the edge area of the membrane in contact with the frame to a substantially uniform high pressure, in an oxygen-free atmosphere.
OBJECTS OF THE INVENTION
One object of this invention is to provide a novel, much lower temperature, diffusian-bonding technique of Pd/40% Cu to copper which avoids flux deterioration, as well as the need for t5 excessive edge gasket compression.
Another object of this invention is a new and improved pure hydrogen-permeating :?o :?5 membrane wall having a Pd/40°'o Cu foil hermetically bonded by such technique to a copper surface on a temperature and pressure-resistant, herein termed "firm", metal frame.
Other and further objects will be; explained hereinafter and are more fully delineated in the appended claims.
SUMMARY OF THE INVENTIOPJ
In summary, from one of its viewpoints, this invention broadly embraces an assembly comprising a thin Pd/40% Cu foill having its edge area diffusion-bonded to a copper-surfaced metallic frame. The term "copper surface" as used in this specification and in the appended SUBSTITUTE SHEET (RULE 26)
4 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 copper-surfaced frame, after exposure to or, preferably in a hydrogen-containing atmosphere, in the range of 200° to 350°
and more particularly between 290° and 325°, for example, for a cycle period of several hours in a hydrogen atmosphere furnace.
no 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, copper surface thereon, and a thin Pd/40% Cu membrane foil having its edge area hermetically sealed to the copper surface by the above diffusion-bonding technique.
t5 Preferred and best made designs and techniques are later presented.
DESCRIPTION OF THE DRAWING
The invention will now be described in connection with the accompanying drawing, the 2o 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 SUBSTITUTE SHEET (RULE 26) 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
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 copper-surfaced frame, after exposure to or, preferably in a hydrogen-containing atmosphere, in the range of 200° to 350°
and more particularly between 290° and 325°, for example, for a cycle period of several hours in a hydrogen atmosphere furnace.
no 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, copper surface thereon, and a thin Pd/40% Cu membrane foil having its edge area hermetically sealed to the copper surface by the above diffusion-bonding technique.
t5 Preferred and best made designs and techniques are later presented.
DESCRIPTION OF THE DRAWING
The invention will now be described in connection with the accompanying drawing, the 2o 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 SUBSTITUTE SHEET (RULE 26) 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
5 pressure and, after exposure to and, preferably in the presence of hydrogen, even when the temperature is in the low range of 200° to 350°C, and preferably between 290° 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.
to 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 co-pending 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-tn:ating. The furnace temperatures were varied between 200°
and 350°C with a slow flow of pure hydrogen gas through the furnace, which was held at atmosphere pressure, or altem;atively under reduced pressure, for about twelve hours.
SUBSTITUTE SHEET (RULE 26) G
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 190° and 325°C 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.
io 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 hydroc,~en 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, diffusion-bonded assemblies deformed badly under gas pressure above about 200°C.
However, operation of such diffusion bonded assemblies below about 200°C is undesirable due to poor hydrogen permeability.
Hence for the purposes of this invention, we use a structurally fimn 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) We have found that diffusion-bonding, as herein described, of a Pd/40% Cu foil to a copper-coating 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) m and/or to too thin a copper plate (ouch 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 5 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 above-described dimensions. Prior to copper plating, they were polished to a smooth finish, some 2o 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.
L7iffusion-bonding of 0.001 inch thick Pd/40% Cu foils to the copper plated frames was then pertormed as above described.
SUBSTITUTE SHEET (R ULE 26) 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)
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.
to 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 co-pending 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-tn:ating. The furnace temperatures were varied between 200°
and 350°C with a slow flow of pure hydrogen gas through the furnace, which was held at atmosphere pressure, or altem;atively under reduced pressure, for about twelve hours.
SUBSTITUTE SHEET (RULE 26) G
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 190° and 325°C 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.
io 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 hydroc,~en 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, diffusion-bonded assemblies deformed badly under gas pressure above about 200°C.
However, operation of such diffusion bonded assemblies below about 200°C is undesirable due to poor hydrogen permeability.
Hence for the purposes of this invention, we use a structurally fimn 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) We have found that diffusion-bonding, as herein described, of a Pd/40% Cu foil to a copper-coating 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) m and/or to too thin a copper plate (ouch 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 5 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 above-described dimensions. Prior to copper plating, they were polished to a smooth finish, some 2o 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.
L7iffusion-bonding of 0.001 inch thick Pd/40% Cu foils to the copper plated frames was then pertormed as above described.
SUBSTITUTE SHEET (R ULE 26) 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 (7)
1 An assembly comprising a thin Pd/40% Cu foil having its edge area diffusion-bonded to a copper-surfaced metallic frame.
2 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 comprising a thin Pd/40% 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.
A method of producing a Pd/40% Cu foil membrane bonded to a copper surfaced metallic frame that comprises exposing said frame and membrane to hydrogen, contacting the edge area of said membrane with said copper frame and applying to said edge area, at a controlled elevated temperature between 200° 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.
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 (1)
Publication Number | Publication Date |
---|---|
CA2337123A1 true CA2337123A1 (en) | 2000-02-03 |
Family
ID=11004731
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002337123A Abandoned CA2337123A1 (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 |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5645626A (en) * | 1990-08-10 | 1997-07-08 | Bend Research, Inc. | Composite hydrogen separation element and module |
JP3540495B2 (en) * | 1996-03-18 | 2004-07-07 | 三菱重工業株式会社 | Hydrogen separation membrane |
-
1998
- 1998-07-23 CA CA002337123A patent/CA2337123A1/en not_active Abandoned
- 1998-07-23 AU AU81258/98A patent/AU755650B2/en not_active Ceased
- 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
-
2001
- 2001-08-13 HK HK01105641A patent/HK1034950A1/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
DE69824452T2 (en) | 2005-06-23 |
HK1034950A1 (en) | 2001-11-09 |
AU8125898A (en) | 2000-02-14 |
DE69824452D1 (en) | 2004-07-15 |
JP3955436B2 (en) | 2007-08-08 |
JP2002521180A (en) | 2002-07-16 |
AU755650B2 (en) | 2002-12-19 |
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