WO1998019812A1 - Multi-channel structures and processes for making such structures - Google Patents
Multi-channel structures and processes for making such structures Download PDFInfo
- Publication number
- WO1998019812A1 WO1998019812A1 PCT/US1997/020418 US9720418W WO9819812A1 WO 1998019812 A1 WO1998019812 A1 WO 1998019812A1 US 9720418 W US9720418 W US 9720418W WO 9819812 A1 WO9819812 A1 WO 9819812A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- mixture
- channel
- rods
- binder
- final assembly
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 183
- 239000000463 material Substances 0.000 claims abstract description 173
- 239000000203 mixture Substances 0.000 claims abstract description 145
- 239000011230 binding agent Substances 0.000 claims abstract description 137
- 239000000945 filler Substances 0.000 claims abstract description 91
- 239000000843 powder Substances 0.000 claims abstract description 65
- 239000002131 composite material Substances 0.000 claims abstract description 57
- 238000005245 sintering Methods 0.000 claims abstract description 42
- 238000010438 heat treatment Methods 0.000 claims abstract description 33
- 239000000919 ceramic Substances 0.000 claims abstract description 29
- 238000001125 extrusion Methods 0.000 claims abstract description 27
- 229910052751 metal Inorganic materials 0.000 claims abstract description 25
- 239000002184 metal Substances 0.000 claims abstract description 25
- 239000003054 catalyst Substances 0.000 claims abstract description 13
- 239000011162 core material Substances 0.000 claims description 64
- 239000007787 solid Substances 0.000 claims description 40
- 239000011257 shell material Substances 0.000 claims description 38
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 36
- 239000012255 powdered metal Substances 0.000 claims description 35
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 33
- 239000012188 paraffin wax Substances 0.000 claims description 30
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 23
- 229910052799 carbon Inorganic materials 0.000 claims description 21
- 239000011159 matrix material Substances 0.000 claims description 18
- 239000000126 substance Substances 0.000 claims description 18
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 17
- 230000008018 melting Effects 0.000 claims description 16
- 238000002844 melting Methods 0.000 claims description 16
- 229920000877 Melamine resin Polymers 0.000 claims description 14
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical group O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 12
- 229910045601 alloy Inorganic materials 0.000 claims description 11
- 239000000956 alloy Substances 0.000 claims description 11
- 239000010949 copper Substances 0.000 claims description 11
- 230000003647 oxidation Effects 0.000 claims description 10
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- 230000001590 oxidative effect Effects 0.000 claims description 10
- 229920000642 polymer Polymers 0.000 claims description 10
- 239000001993 wax Substances 0.000 claims description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 9
- 229910002804 graphite Inorganic materials 0.000 claims description 9
- 239000010439 graphite Substances 0.000 claims description 9
- 229910002543 FeCrAlY Inorganic materials 0.000 claims description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 8
- 229910052802 copper Inorganic materials 0.000 claims description 8
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical group [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 8
- 239000000395 magnesium oxide Substances 0.000 claims description 7
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 7
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 6
- 239000004202 carbamide Substances 0.000 claims description 6
- RUDFQVOCFDJEEF-UHFFFAOYSA-N yttrium(III) oxide Inorganic materials [O-2].[O-2].[O-2].[Y+3].[Y+3] RUDFQVOCFDJEEF-UHFFFAOYSA-N 0.000 claims description 6
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 5
- 229910052721 tungsten Inorganic materials 0.000 claims description 5
- 238000009835 boiling Methods 0.000 claims description 4
- 239000000292 calcium oxide Substances 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 229910052697 platinum Inorganic materials 0.000 claims description 4
- 239000010937 tungsten Substances 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 239000012254 powdered material Substances 0.000 claims description 2
- 229920001169 thermoplastic Polymers 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims 6
- 239000012815 thermoplastic material Substances 0.000 claims 3
- 239000003575 carbonaceous material Substances 0.000 claims 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 1
- 229910052737 gold Inorganic materials 0.000 claims 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims 1
- 229910052709 silver Inorganic materials 0.000 claims 1
- 239000004416 thermosoftening plastic Substances 0.000 claims 1
- 238000009834 vaporization Methods 0.000 claims 1
- 230000008016 vaporization Effects 0.000 claims 1
- 229910000765 intermetallic Inorganic materials 0.000 abstract description 5
- 150000002739 metals Chemical class 0.000 abstract description 5
- 239000000969 carrier Substances 0.000 abstract description 3
- 239000002904 solvent Substances 0.000 abstract 1
- 239000000835 fiber Substances 0.000 description 19
- 239000002245 particle Substances 0.000 description 12
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 10
- 235000013871 bee wax Nutrition 0.000 description 10
- 239000012166 beeswax Substances 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 8
- -1 polyethylene Polymers 0.000 description 7
- 239000004698 Polyethylene Substances 0.000 description 6
- 229920000573 polyethylene Polymers 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- 229910010271 silicon carbide Inorganic materials 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 238000007711 solidification Methods 0.000 description 4
- 230000008023 solidification Effects 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 238000007596 consolidation process Methods 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 229910001092 metal group alloy Inorganic materials 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000000280 densification Methods 0.000 description 2
- 230000005496 eutectics Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000011174 green composite Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 229910000907 nickel aluminide Inorganic materials 0.000 description 2
- 230000006911 nucleation Effects 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- QLZJUIZVJLSNDD-UHFFFAOYSA-N 2-(2-methylidenebutanoyloxy)ethyl 2-methylidenebutanoate Chemical compound CCC(=C)C(=O)OCCOC(=O)C(=C)CC QLZJUIZVJLSNDD-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000005524 ceramic coating Methods 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000000641 cold extrusion Methods 0.000 description 1
- 238000009694 cold isostatic pressing Methods 0.000 description 1
- 238000005097 cold rolling Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
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- 239000000470 constituent Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 description 1
- 239000005042 ethylene-ethyl acrylate Substances 0.000 description 1
- 239000003733 fiber-reinforced composite Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229910000856 hastalloy Inorganic materials 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
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- 150000001247 metal acetylides Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
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- 238000004663 powder metallurgy Methods 0.000 description 1
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- 238000002360 preparation method Methods 0.000 description 1
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- 239000002994 raw material Substances 0.000 description 1
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- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
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- 239000002887 superconductor Substances 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
- B01D39/2072—Other inorganic materials, e.g. ceramics the material being particulate or granular
- B01D39/2075—Other inorganic materials, e.g. ceramics the material being particulate or granular sintered or bonded by inorganic agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
- B01D63/066—Tubular membrane modules with a porous block having membrane coated passages
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/08—Hollow fibre membranes
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/10—Sintering only
- B22F3/11—Making porous workpieces or articles
- B22F3/1103—Making porous workpieces or articles with particular physical characteristics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/10—Sintering only
- B22F3/11—Making porous workpieces or articles
- B22F3/1121—Making porous workpieces or articles by using decomposable, meltable or sublimatable fillers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/10—Sintering only
- B22F3/11—Making porous workpieces or articles
- B22F3/1121—Making porous workpieces or articles by using decomposable, meltable or sublimatable fillers
- B22F3/1134—Inorganic fillers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B18/00—Layered products essentially comprising ceramics, e.g. refractory products
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/04—Constructions of heat-exchange apparatus characterised by the selection of particular materials of ceramic; of concrete; of natural stone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/32—Component parts, details or accessories; Auxiliary operations
- B29C43/36—Moulds for making articles of definite length, i.e. discrete articles
- B29C2043/3665—Moulds for making articles of definite length, i.e. discrete articles cores or inserts, e.g. pins, mandrels, sliders
- B29C2043/3668—Moulds for making articles of definite length, i.e. discrete articles cores or inserts, e.g. pins, mandrels, sliders destructible or fusible
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/006—Pressing and sintering powders, granules or fibres
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/65—Aspects relating to heat treatments of ceramic bodies such as green ceramics or pre-sintered ceramics, e.g. burning, sintering or melting processes
- C04B2235/656—Aspects relating to heat treatments of ceramic bodies such as green ceramics or pre-sintered ceramics, e.g. burning, sintering or melting processes characterised by specific heating conditions during heat treatment
- C04B2235/6562—Heating rate
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/65—Aspects relating to heat treatments of ceramic bodies such as green ceramics or pre-sintered ceramics, e.g. burning, sintering or melting processes
- C04B2235/656—Aspects relating to heat treatments of ceramic bodies such as green ceramics or pre-sintered ceramics, e.g. burning, sintering or melting processes characterised by specific heating conditions during heat treatment
- C04B2235/6567—Treatment time
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/30—Composition of layers of ceramic laminates or of ceramic or metallic articles to be joined by heating, e.g. Si substrates
- C04B2237/32—Ceramic
- C04B2237/34—Oxidic
- C04B2237/343—Alumina or aluminates
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/30—Composition of layers of ceramic laminates or of ceramic or metallic articles to be joined by heating, e.g. Si substrates
- C04B2237/32—Ceramic
- C04B2237/34—Oxidic
- C04B2237/345—Refractory metal oxides
- C04B2237/348—Zirconia, hafnia, zirconates or hafnates
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- C—CHEMISTRY; METALLURGY
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- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/30—Composition of layers of ceramic laminates or of ceramic or metallic articles to be joined by heating, e.g. Si substrates
- C04B2237/32—Ceramic
- C04B2237/36—Non-oxidic
- C04B2237/365—Silicon carbide
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- C—CHEMISTRY; METALLURGY
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- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/50—Processing aspects relating to ceramic laminates or to the joining of ceramic articles with other articles by heating
- C04B2237/62—Forming laminates or joined articles comprising holes, channels or other types of openings
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- C—CHEMISTRY; METALLURGY
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- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/50—Processing aspects relating to ceramic laminates or to the joining of ceramic articles with other articles by heating
- C04B2237/66—Forming laminates or joined articles showing high dimensional accuracy, e.g. indicated by the warpage
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2237/00—Aspects relating to ceramic laminates or to joining of ceramic articles with other articles by heating
- C04B2237/50—Processing aspects relating to ceramic laminates or to the joining of ceramic articles with other articles by heating
- C04B2237/76—Forming laminates or joined articles comprising at least one member in the form other than a sheet or disc, e.g. two tubes or a tube and a sheet or disc
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/60—Construction of the column
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/60—Construction of the column
- G01N30/6034—Construction of the column joining multiple columns
- G01N30/6043—Construction of the column joining multiple columns in parallel
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/60—Construction of the column
- G01N30/6052—Construction of the column body
Definitions
- the present invention relates to novel methods for producing multi-channel structures and to structures produced by such methods that are suitable for uses as filters, catalyst carriers, heat exchangers, etc., especially such structures having relatively small channels or apertures ranging from a few microns to a few millimeters in diameter.
- Bubbles which form in the liquid float to a hotter region and are reabsorbed. Bubbles which form at the solid-liquid interface may grow as either isolated or continuous porosity, depending on the solidification conditions.
- the final microstructure of the porous materials depends on both thermodynamic and kinetic processes. Homogeneous nucleation of bubbles under GASAR processing conditions is impossible, the process is limited to systems which do not form hydrides, the eutectics are highly asymmetric, which leads to an extremely small range of compositions and solidification temperatures where stable eutectic growth is possible.
- This method does not allow the manufacture of long structures with through microchannels of a given diameter. Moreover, this method cannot be used for producing channels oriented in two or more desired directions.
- U.S. Patent 4,818,264 issued April 4, 1989 to Marsha L. Langhorst discloses that hollow glass fibers have been made by drawing down tubes which can be used to produce glass polycapillary materials. Seven glass tubes, 1.8mm outside diameter by 1.4mm inside diameter, were placed inside an 8 mm outside diameter by 6mm inside diameter glass tube and this assembly was drawn with a glass tube drawing machine.
- the subject patent cites an article by H. D. Pierce Jr. Et al, Technical note "A method for the Preparation of Glass Multicapillary Columns", vol. 17, J. of Chromatographic Science, 5/79, 297, as the source of this work. This method cannot be applied to the powder or brittle materials, such as ceramics, intermetallics, carbon, etc.
- Extrusion method for forming thin-walled honeycomb structures was developed by D. Rodney et al. as disclosed in U.S. Patent No. 3,790,654 issued February 5, 1974.
- Rodney et al. disclose the use of an extrusion die having an outlet face provided with a gridwork of interconnected discharge slots and inlet face provided with a plurality of feed openings extending partially through the die in communication with the discharge slots.
- Extrudable material is fed to the die under pressure wherein the extrudable materials flow to the interconnected discharge slots communicating with the outlet face, wherein a portion of the material flows laterally within such slots to form a continuous mass before being discharged longitudinally therefrom to form a thin-walled structure having a multiplicity of open passages extending therethrough.
- the longitudinally discharged mass is rigidified to prevent deformation of the passages.
- the disadvantage of this method is a very complicated and very expensive tooling, which does not allow the production of the channels less than 0.5-1 mm in diameter and interchannel walls less than 0.2 mm in diameter, nor does it allow the production of structures with channels oriented in two or more directions.
- some of the procedures used in carrying out the present invention to produce channeled structures are also used in making monolithic fibrous ceramic structures, as described in U.S. Patent No. 4,772, 524 issued September 20, 1988 to William S. Coblenz.
- the Coblenz patent discloses a method of producing fibrous monolithic ceramic product of high density.
- This product is formed of a plurality of coated fibers and each coated fiber comprises a ceramic core with a ceramic coating.
- the green body of ceramic materials from which the product is formed is plastically deformed and densified by sintering.
- there is no disclosure or suggestion in this patent for using procedures to produce a multi-channeled structure such as that disclosed and claimed herein.
- U.S. Patent No. 4, 965, 245, issued October 23, 1990 to Masaru Sugimoto et al. discloses a method of producing a superconducting cable or coil comprising a bundle of coated metallic filaments, for example, coated with an oxide, that are drawn and heated in oxidizing atmosphere to form a superconductor. Again, this patent neither discloses nor suggests a process for making channeled structures as disclosed and claimed herein.
- a multi-channel structure comprising a body of structural material having a plurality of channels therein is produced by forming a composite rod comprising an outer shell formed of a powdered form of the structural material and a binder material and an inner core formed of a powdered form of a removable channel forming filler material and a binder material, assembling a first bundle of said composite rods in parallel relationship, consolidating said first bundle and reducing the diameter of the individual rods in said first bundle by deforming said first bundle, assembling a plurality of said deformed first bundles with a further bundle of said first bundles and consolidating the further bundle into a final assembly.
- the binder is then removed from both the outer shell material and the filler core material.
- the filler core material is removed and the resulting structure is sintered to produce the final structure containing channels as defined by the removed filler material of the cores of the respective composite rods of the final assembly of bundles.
- the binder and filler core material may be removed before sintering, during the sintering process or after sintering, for example, by evaporation, decomposition, dissolution, infiltration, melting with following blow out, etc.
- Certain filler core materials e.g., carbon, may be removed by oxidation and burning.
- the structural material is a sinterable ceramic powder, such as alumina;
- the channel forming filler of the core is graphite powder or melamine or urea or a polymer, such as polyethylene or polypropylene;
- the binder of both the core and outer shell is paraffin or wax.
- the viscosity or yield points of shell and core mixtures at extrusion temperature should be as close as possible to one another.
- the binder is removed by heating.
- the binder should have a melting or boiling point below that of the filler core material, or below the oxidizing point of the filler core material when such material is carbon and the heating is done in an oxidizing atmosphere.
- the filler core material can also be removed by heating or by oxidation through heating at a higher temperature after removal of the binder, and this can be accomplished during the application of the heat used to perform the sintering step, which will require higher temperature than the melting or boiling point or oxidation point of the filler material.
- the structural material of the shell is formed of a powdered metal, such as tungsten or iron powders
- the channel forming filler material of the core is a low melting point metal powder, such as copper.
- the binder has an essentially lower melting point than the core filler and may be paraffin or polyethylene or a mixture of several substances.
- the structural materials of the shell is formed of a metal alloy such as FeCrAlY or Hastealloys powders, and the channel forming filler material of the core is low carbon residue polymer such as melamine.
- the binder may be wax and the filler and the binder materials may be removed partially or completely by organic solvent and/or by evaporation, before or during sintering.
- the composite rod inner core is formed of at least one filler- binder rod formed of the channel forming filler material and the binder
- the outer shell is formed by positioning a plurality of rods formed of the mixture of structural and binder materials disposed around and parallel to the core to form a bundle which is deformed, for example, by extrusion to form the composite rod for practicing the method as described above.
- the structural material of the shell is formed of a non-carbide forming powdered metal, such as precious metal powders as platinum, palladium, etc. or non- carbide forming metal powders such as magnesium, copper and nickel, and non-carbide forming alloys such as nickel aluminide, and the channel forming filler material of the core is powdered carbon.
- the binder has an essentially lower melting point than the oxidation point of the carbon core filler, and may be paraffin or a wax.
- the oxidation of the carbon filler material is controlled by maintaining it in a non-oxidizing atmosphere such as nitrogen or argon while heating the resulting structure to remove the binder, as by melting it, and the temperature of the structure is maintained until the structural components of the structure bond or link to one another to maintain its structural integrity.
- a non-oxidizing atmosphere such as nitrogen or argon
- the non-oxidizing atmosphere is removed and replaced by an oxidizing atmosphere, such as oxygen or air, in order to remove the carbonaceous filler by oxidation, i.e., burning. This may be done apart from or in the course of raising the applied heating temperature to that required for the sintering step.
- the methods of the present invention enable the production of novel structures with channels that are of smaller diameter than those of prior methods and also with channels that are formed with relatively thin interchannel walls.
- novel methods of the present invention are simpler and less complex to perform than those of the prior art discussed above which requires the use of relatively expensive equipment including more complex dies, as compared to the simple single orifice dies that can be employed to practice the present invention, to produce structures with a plurality of channels of relatively small diameter.
- This method can be used to produce porous polycapillary structures of different ceramics, intermetallics, and metals.
- This technique allows control of the final porosity (from a few volume percent to 90 vol.% and more) channel diameter and interchannel wall thickness (from a few microns to a few millimeters) with small tolerance.
- This technique can produce not only unidirectional channel structure, but can be adapted to produce bi-directional and three dimensionally porous structures as well.
- FIGURES Figure 1 is a schematic representation of the steps involved in producing a multichannel structure according to the present invention.
- Figure 2 is a schematic representation of a procedure comprising a cross sectional view of another embodiment of the composite rod shown in step 1 of Figure 1.
- Figure 3 is a schematic representation of a cross sectional view of still another embodiment of the composite rod shown in step 1 of figure 1 , wherein an additional layer comprised of a second structural matrix-binder mixture 12A is interposed between the outer structure matrix-binder layer 12 and the inner core 13.
- Figure 4 is a schematic representation showing another embodiment of the final assembly of bundles 19 illustrated in step 4 of Figure 1 for producing a structure with channels oriented in two perpendicular directions and having different diameters.
- Figures 5a and 5b show the other embodiment of step 4 of Figure 1 arranged to produce a large channel surrounded by multi-channel structure ( Figure 5 a) and to produce a solid central structure surrounded by multichannel structures (Figure 5b)
- FIG. 1 there is shown a cross-sectional view of a composite rod 11, comprising an outer shell 12 formed of a first mixture comprised of a powdered form of a structural material such as alumina, and a binder material such as paraffin, and an inner core 13 formed of a second mixture comprised of a powdered form of a channel forming filler material such as melamine or graphite, and a binder such as paraffin.
- a composite rod 11 comprising an outer shell 12 formed of a first mixture comprised of a powdered form of a structural material such as alumina, and a binder material such as paraffin, and an inner core 13 formed of a second mixture comprised of a powdered form of a channel forming filler material such as melamine or graphite, and a binder such as paraffin.
- the composite rod 11 may be formed, for example, by first producing a tube of the first mixture, for example by extrusion, to form the outer shell 12.
- the inner core 13 may be separately formed of the second mixture, for example by extrusion.
- the composite rod 11 may then be formed by inserting the inner core 13 into the shell 12.
- the mixtures comprising the materials to form the outer shell 12 and the inner core 13 may simultaneously be extruded using a concentric two-channel die to form the composite rod 11.
- the composite rod 11 Once the composite rod 11 is formed, as above, it can be further reduced in diameter, if desired, by extrusion to reduce its diameter to that illustrated as 11A in Figure 1.
- a bundle 14 of composite rods (11 or 11 A) is then assembled as per step 2 illustrated in Figure 1, wherein the composite rods shown as 11A are disposed parallel to one another, in cross section.
- a convenient way of producing the several parallel rods (11 A) is to produce a long composite rod (11) that may be cut into segments, either before or after reduction in diameter, to 11 A, to form the various parallel rods to form the bundle 14.
- the bundle 14 of assembled rods is then subjected to deformation, as by extrusion, per step 2 in an extruder 15, shown in cut-away side view, and which has an appropriately sized diameter die to deform and reduce the diameter of the bundle 14, to that shown as bundle 14A as well as the diameter of the individual composite rods 11A comprising the reduced diameter bundle 14A.
- a further bundle 17 may be assembled of a plurality of parallel bundles 14A containing the further reduced diameter composite rods 11B.
- This further bundle 17 is then subjected to further deformation as per extruder 18, which is provided with a die of appropriate diameter to reduce further the diameter of the further bundle 17 to smaller diameter 17A, as shown per step 3.
- the extruder used in steps 1, 2 or 3 may be the same equipment, suitably provided with an extrusion die of the diameter desired for the respective step.
- the procedure of assembling bundles of composite rods and deforming those bundles as by extrusion to reduce the diameter of the bundles as well as their constituent composite rods, thereby reducing the diameter of the individual cores 13 and increasing their number per given volume, can be carried out until the desired diameter and number of channel-forming cores is achieved.
- the deformation of the assembled bundle of composite rods constitutes a consolidation of the numbers of the bundle, into a rod that may be of circular cross sectional configuration or rectangular or other form.
- the final assembly of bundles 17A may, for example, comprise a large bundle assembled in a die 21 for consolidation by compression within the die 21 by a plunger 22, per step 4.
- the consolidated bundle 19 is then subjected to heat treatment per step 5, which includes removing the binder i.e. debinding, and removing the filler material as well as sintering of the remaining multi-channel green body structure comprised of the channeled structural material.
- the selection of the filler is dependent on the type of structural materials in that the filler should remain in place until sufficient mechanical integrity develops in the structural material, but it should be removed under conditions that do not deteriorate the properties of the structural materials.
- the filler material should be chemically compatible with the structural material over the temperature range both in existence. Filler that remains to relatively high temperature before it is removed will have a wide range of applicability to a variety of structural materials. For example, MgO, CaO, etc. will not be removed during the process of sintering, they allow for the holding of the shape of the channels during sintering, and they can be removed by dissolution after sintering.
- fillers for high temperature refractory metals such as W, Ta, and the like, when the development of sufficient structural integrity of the shell require temperatures as high as 800 to 1200°C.
- filler material should not form new undesirable compounds with the structural material. If low temperature polymer is used which is removed before structural materials develop sufficient mechanical integrity, the multi-channel structure could be unstable and collapse. It is possible to use lower melting temperature filler, but in that case, the filler removal should be conducted very slowly in the powder bed to support the structure.
- Structural materials that require relatively high temperature before it develops sufficient mechanical integrity such as alumina, silicon carbide, and nickel especially benefit from the use of a carbon filler material.
- Carbon filler can be used with the structural materials, which don't form carbides and other chemical compounds in the process of debinding, sintering and filler removing, excluding the cases when their occurrence is envisaged.
- the chemical composition of the channeled structural materials will typically be that of the starting structural powder materials used to form the composite rods.
- desired chemical composition of structure materials can also be obtained by starting with mixed structural powders and causing the powder to react during or after sintering to form the desired composition.
- metal alloys such as FeCrAlY, which is a high temperature alloy with high room temperature ductility and exceptional cyclic oxidation resistances and excellent shock resistance which are properties that make this alloy an excellent catalyst support for high temperature applications, can be made from the corresponding alloy powders or by mixing at the appropriate stoichiometric ratio the corresponding elemental metal powdered components of the alloys, and forming the alloy in-situ during or after sintering by applying heat to cause the elemental metal component to form the desired alloy.
- catalyst such as platinum can be applied by dip coating or electrodeposition to form the catalyst product for such applications as catalytic converters.
- the catalyst such as platinum can be incorporated as one of the powdered components of the structural material that is used to form the composite rods.
- the same methods can be applied to form desired intermetallics such as nickel aluminide from nickel and aluminum powders.
- this method can be used to form ceramic compositions such as silicon carbide from silicon and carbon powders in multi-channel structural material. This technique allows for starting with less costly raw materials with the desired properties such as particle size.
- the process consists of the following steps (Figure 1):
- Step 1 Production of bi-material rods. 11, consisting, for example, of shell (alumina + binder) and core (filler + binder).
- the shell comprises a mixture of alumina powder with a binder additive (wax, paraffin, or some thermoplastic polymer like ethylene vinyl acetate, ethylene ethyl acrylate, etc.).
- the core comprises a mixture of the binder with a powder of channel-forming filler which can be removed afterwards by evaporation, melting, dissolution, oxidation, etc.
- the powders of carbon like graphite or amo ⁇ hous carbon
- other organic like urea, melamine, polymers
- inorganic like CaO, MgO, metals
- Step 2 Assembling the rods into a bundle and re-extruding the bundle:
- a green composite blank that comprises of matrix (alumina + binder) and channel -forming fibers (filler + binder) will be obtained.
- the fibers produced by this stage of extrusion may still have too large a diameter - up to a few hundred microns, hence further reduction in scale may be necessary.
- Step 3 Repeating step 2 for further refinement in scale of channels: At the conclusion of this step, the rods obtained will have diameters of 0.1-10 mm, with channel- forming fibers of a diameter of 10-100 microns, depending on the extrusion ratio. This step can be repeated, if necessary, to get even smaller diameter fibers.
- Step 4 Assembling the rods produced in step 3 into a bundle and their consolidation in a die, or by cold isostatic pressing, cold extrusion, cold rolling, etc., in order to get the desired green density prior to hot-densification.
- Step 5 - Densification includes sequentially (1) removing the binder, (2) removing the filler, and (3) sintering the multi-channel alumina green body.
- the sintering occurs in such a manner that thermally-induced cracks are avoided and provides high density of the interchannel walls in order to get high strength of filter.
- paraffin is used as binder, its removal will occur at 150-350°C.
- temperatures of about 300-500°C are required.
- Sintering of alumina will occur at 1500 - 1700°C.
- a bi-material rod with core diameter 0.5 mm and shell diameter 1 mm can be obtained at stage 1 . Then, on the stage 2, a bundle of 1000 of these rods should be collected and extruded from diameter 36mm to diameter 1 mm, so after stage 2, we will have a diameter of fibers from filler + binder mixture (and hence future channels) in this rod of ⁇ 20 micrometers. Step 3 in this case can be excluded. Rods obtained in step 2 should be bundled, pressed (step 4), and sintered (step 5). If smaller diameter channels are required, step 3 may be reincluded.
- the method of this invention is to use repeated coextrusion of a rod structure comprised of a removable inner core comprised of a mixture of filler and binder powders and an outer shell comprised of a mixture of binder powder and of sinterable structural powder material to form a fiber reinforced ceramic matrix green blank to be followed by debinding, removal of the fibers found by the filler material and sintering of the matrix.
- a rod structure comprised of a removable inner core comprised of a mixture of filler and binder powders and an outer shell comprised of a mixture of binder powder and of sinterable structural powder material to form a fiber reinforced ceramic matrix green blank to be followed by debinding, removal of the fibers found by the filler material and sintering of the matrix.
- Step 1 a first mixture of 85 weight % alumina powder (aver, particles diameter 1.3 ⁇ m) and 15 wt% paraffin, a binder, was prepared. This first mixture was heated at 90°C and blended.
- Step 2 a second mixture of 79 wt% melamine powder (aver, particle size 2.5 uk) and 21 wt% paraffin binder was prepared like the mixture in step 1.
- Step 3 The two mixtures prepared in step 1 and step 2 were loaded in the 2-channel extruder and extruded at 45°C. As a result, bi-material rods, having a core of 1 mm in diameter and sheath 2 mm in diameter were produced.
- the core consisted of the second mixture of melamine powder with paraffin and the sheath consisted of the first mixture of alumina powder with paraffin.
- Step 4 The bi-material rods obtained in step 3 were cut into 100 mm segments, and a bundle of 631 such segments was assembled, and the bundle, which was in substantially parallel relationship was inserted into the die, which had a container 90 mm in diameter and outgoing hole 3 mm in diameter, and extruded.
- the rod 3 mm in diameter was produced that had the structure of fiber reinforced composite with matrix of mixture alumina powder and paraffin binder and with 631 fibers comprised of mixture of melamine powder with paraffin binder.
- the diameter of each fiber was approximately 60 micrometers.
- Step 5 The bundles of rods obtained in step 4 were cut into 50 mm length segments and 300 such segments were stacked in parallel relationship into a rectangular 50x90 mm die (10 layers, each layer of 30 segments), then the stack was pressed at 40°C (pressure 1500 N/c ⁇ r) in order to consolidate the stack of rods. As a result, the rectangular green (i.e., uncured) composite structure having 189300 fibers was obtained.
- Step 6 The green body structure obtained in step 5 was heated and sintered.
- the procedure of the heat treatment was as follows: heating while raising the temperature from 20°C to 250°C at a rate of 5°C/hour, hold the upper temperature for 0.5 h, then continue heating while raising the temperature to 350°C at a rate of 15°C/h, hold the upper temperature for 1 h, then continue heating while raising the temperature to 540°C/h, hold for 1 hr, heating to 815°C with rate
- Step 1 - Bi-material rods consisting of the 1 mm outer diameter shell, which comprises a first mixture of tungsten powder (average size of particles - 5 micrometers) with 48 vol% binder (34% paraffin wax, 33% polyethylene wax and 33% beeswax) and of the 2.5 mm diameter core comprises a second mixture of 5 micrometers copper powder with 60 vol% of the same binder were produced by extrusion of 60mm diameter bi-material green body into diameter 4 mm.
- Step 2 - 169 bi-material rods, obtained in step 1 were assembled in substantially parallel relationship into a bundle, which was inserted into 60 mm barrel and extruded through a 2 mm diameter die.
- a bundle of 2 mm diameter green composite rods comprised of (W + binder) matrix and 169 (Cu + binder) fibers, having diameter ⁇ .1 mm were obtained.
- Step 3 The bundles of 2 mm rods, produced in the step 3, were cut into segments 50 mm length, these bundles of segments were placed in the square die 50 x 50 mm, and pressed with a force of 6000 kgf in order to consolidate the assembled rods.
- Step 4 The green body (i.e., uncured structure), obtained after step 3 was heated in H, atmosphere from 20°C to 500°C at the rate of 0.2°C/min. for the binder removal, then heated in a hydrogen atmosphere at temperatures ranging from 500°C to 1280°C with a rate of 5°C/min.
- Cu starts to melt at 1083°C, infiltrates the W matrix and leaves channels instead of fibers.
- the interchannel walls that comprise the resulting structure consist of W- Cu pseudoalloy.
- Step 1 Bi-material rods, consisting of the 1 mm outer diameter shell, which is comprised of a first mixture of carbonyl Fe powders with 40 vol% binder (85% paraffin and 15% beeswax), and of the 0.81 mm diameter core comprised of a mixture of melamine powder with 50 vol% the same binder, were produced by extrusion of 60 mm diameter bi-material green body (54 mm diameter core of melamine with binder and 60 mm diameter shell of Fe with binder) into diameter 1 mm.
- Step 2 The rods obtained in step 1 were cut to segments 100 mm length and a bundle of 1027 bi-material segments was assembled into a bundle of parallel rods which was isopressed at 45°C at pressure 10 MPa in order to consolidate the assembled rods.
- Step 3 The green body ⁇ 30 mm obtained after step 2 was heated in an atmosphere of H 2 with temperature raised from 20°C to 500°C at a rate of 0.2°C/min. in order to remove the binder and melamine, then sintered by being heated in an atmosphere of H 2 from a temperature raised from 500°C to 1200°C at a rate of 5°C/min and held at 1200°C for two hours.
- the resulting structure of iron comprising a rod ⁇ 87 mm length and 25 mm diameter with 1027 channels of 0.66 mm diameter was produced.
- Step 1 A first mixture of 63 vol% alumina powder (aver, particle size ⁇ 1.3um) and 37 vol% binder (80% paraffin + 20% polyethylene) was prepared.
- Step 2 A second mixture of 60 vol% magnesia powder (aver, particle size ⁇ 1.8um) and 40 vol % binder (80% paraffin + 20% polyethylene) was prepared.
- Step 3 The 2 mixtures prepared in steps 1 and 2 were loaded in the two-channel extruder with the first mixture arranged to be extruded as the outer shell over the first mixture as an inner core and extruded at 55°C. As a result, bi-material rods having core 2 mm in diameter and shell 4 mm in diameter, were produced.
- the cores consisted of the second mixture (magnesia + binder) and the shell consisted of the first mixture (alumina + binder).
- Step 4 Bi-material rods obtained in step 3 were bundled, inserted into the die which had a container 90 mm in diameter and outgoing hold 20 mm in diameter, and extruded. As a result, the 20 mm diameter green body rod structure with 91 future channels was produced.
- Step 5 The green body structure obtained in step 5 was heated and sintered.
- the procedure of the heat treatment was as follows: heating from 20°C to 500°C at a rate of 5°C/hr, then heating from 500°C to 1100°C at a rate
- Step 6 A piece of the sintered structure obtained in the step 5 was cut into segments 20 mm in length, the segments were placed into HN0 3 at 60°C and held there for 6 hours. MgO fibers were dissolved from the structure and left channels ⁇ 1 mm in diameter in the remaining structure.
- alumina powder with 1.3um particle size were mixed with 50 vol% binder (paraffin wax/beeswax) to give a viscous mixture at ⁇ 45-50°C.
- this mixture was extruded through a 12 mm die, connected to a 60 mm container.
- 12 mm rod was produced out of alumina-binder mixture and cut into smaller pieces ( ⁇ 100 mm each).
- the filler-binder mixture was prepared out of melamine powder (50 vol%) and a binder (paraffin wax beeswax) and this filler-binder mixture was extruded into the same sized 12 mm rods.
- the rods of alumina-binder and filler-binder were arranged into a bundle with one filler-binder rod in the middle and two concentric layers around it - the first layer comprising filler-binder rods and the second (external) layer comprising alumina-binder rods.
- the green body structure comprised of a bundle of 12 mm rods with 19 filled passages - was embedded into fine alumina powder and heat treated in the air.
- the alumina powder removes the liquefied binder by capillary action during the heat treatment which caused the wax binder to melt.
- the de-binding process was conducted with 5-6°C hr. heating rate, 2 hr. hold time, then heating the sample up to 1100°C with 30-35°C/hr heating rage, 2 hr. hold time and cooling down with the furnace. After the sample was removed from the embedding powder, it was further sintered at 1400°C with slow heating rate and 2 hr. hold time. Note that we have also used carbon powder in place of the Alumina powder to absorb the liquefied binder.
- an alumina structure sample comprising 19 channels was produced.
- the OD after sintering was 9.3 mm and the channel size ⁇ 1.6 mm with the volume fracture of channels of about 69% and 1 mm wall thickness between the channels.
- the bi-material rods were cut into 19 pieces and arranged in a bundle consisting of one filler- binder rod in the center and two concentric layers around with 6 and 12 rods in them, respectively.
- the first concentric layer was comprised of filler-binder rods and the second (external) layer was comprised of Zr0 2 Y 2 0 3 -binder rods.
- the bundle was inserted into a 60 mm container and extruded through a 12 mm die to produce a rod structure comprising a Zr0 2 /Y 2 0 3 matrix and 19 2.4 mm passages filled with the filler matrix.
- the high temperature metal alloy, (FeCrAlY) multi-channel rod with 85% volume loading of channels and channel diameter of ⁇ 0.5 mm was produced in the following manner: Powder of Fe-25Cr-5Al-0.5Y was mixed with 45 vol% binder (paraffin wax eeswa ), the mixture was extruded through a 5 mm die and the obtained rod was cut into segments 100 mm long and 5 mm diameter.
- Binder paraffin wax eeswa
- the filler-binder mixture was prepared out of melamine powder (50 vol%) and a binder (paraffin wax/beeswax). After extrusion, the rod of this filler- binder mixture of diameter 55 mm was obtained.
- the parallel rods of FeCrAlY-binder and filler-binder were arranged into a parallel bundle with one filler-binder rod in the middle and one concentric external layer comprising fecralloy-binder rods around it. After extrusion of this bundle through the 0.75 mm die at 45°C, a bi-material rod was obtained with an FeCrAlY-binder shell and filler-binder in the middle.
- the rod was cut into 40 mm segments long which were assembled in a bundle of 1000 parallel segments, the bundle was loaded into the die of rectangular cross-section 40x30 mm and compacted under pressure 15 MPa at temperature 45°C.
- a green body 40x30x12 mm comprising a FeCrAlY-binder matrix with 1000 uniformly distributed parallel filler-binder fibers was obtained.
- Debinding and sintering was carried out to remove binder and filler and as a result, the preassigned multi-channel FeCrAlY structure with 1000 channels oriented pe ⁇ endicular to the plane 40x12 mm is obtained.
- the debinding was carried out by slow heat (0.1°C/minute) to 350°C followed by holding for 10 hours, and the sintering was carried out by heating from 350°C to 1400°C at a rate of 0.2°C/min in an ultrapure hydrogen atmosphere, with 2 hours holding at 1400°C.
- the 40x30x12 mm multi-channel green bar of superalloy Hastelloy X was manufactured. It had 85% volume fraction of channels of 0.5 mm diameter.
- the powdered mixture Ni-45%, Cr-22%, Fe-18%, Mo-9%, Co-1.5%, W-0.5% was used as the structural material. It was mixed with the 50 vol% of binder comprising 85% paraffin and 15% beeswax and the mixture obtained was used as shell of bi-material rod.
- the core of the rod was made of a mixture of 55% melamine + 50% the same binder. Procedure of manufacturing green body was the same as in the Example 8.
- alumina powder with an average particle size of 1.3 micron was mixed with a mixture of paraffin plus beeswax binder.
- the binder contains 90% paraffin and 10% beeswax.
- the mixture contains 50% binder and 50% alumina powder.
- the filler mix was prepared by mixing graphite powder with an average particle size of 20 micron with the same binder as previously described.
- the loading being 50% binder and 50% graphite.
- a tube of the first mixture was extruded to a 60 millimeter outside diameter and 30 millimeter inside diameter.
- a rod of the second mixture was extruded that was 30 millimeter in diameter. This was inserted in the tube made from the first mixture.
- This composite rod composed of the alumina-binder tube, which formed the outer shell, and the graphite-binder rod, which formed the core, was extruded in a die to make a 2 millimeter composite rod.
- This 2 millimeter composite rod was cut into segments 100 millimeter long.
- a bundle of 631 segments were assembled and inserted into a die which had a container and a 90 millimeter diameter cavity and a 30 millimeter outgoing hole and was then extruded.
- the result is a green body (composite) structure of 30 millimeter outside diameter and with 631 filler graphite and binder fibers having diameter of 0.3 millimeters.
- This composite structure was then heated from room temperature to 400°C at a rate of 0.1 °C per minute for debinding.
- the composite structure was heated from 400°C to 1600°C at a rate of 1.0°C per minute and held for 2 hours at 1600°C for the burn out of the graphite filler and the sintering of the alumina structure.
- the first mixture was prepared out of 52 vol% sinterable silicon carbide powder with particle size 0.5 micron and 48 vol% binder consisting of 70 wt% polyethylene wax, 25 wt% paraffin wax and 5 wt% beeswax.
- the second mixture was prepared out of 50 vol% graphite powder (Asbury brand, grade No. Micro 850, particle size -325 mesh) and 50 vol% of the same binder.
- the first mixture was extruded through a 20 mm die connected to a 60 mm container to produce 20 mm rods.
- the second mixture was extruded the same way to produce similar 20 mm rods.
- the rods were assembled into a bundle comprising 7 rods: one - out of second mixture - in the middle, surrounded by six rods made out of first mixture, and inserted into a 60 mm container followed by the extrusion through the attached 20 mm die.
- the composite rod produced during the previous step was cut into 7 pieces of a given length, assembled into a bundle, inserted into a 60 mm container and extruded again through the attached die to produce a further rod with a composite structure: the matrix made out of silicon carbide mixed with binder and seven fibers made out of graphite powder mixed with binder.
- this composite rod was cut into seven pieces as well, bundled, inserted into a die container and extruded through the same die.
- a green body structure comprising a silicon carbide/binder matrix and 49 graphite/binder fibers was produced.
- the heat treatment consisted of two steps: (1) de-binding (imbedding media - graphite); at 350°C for 5 hr. at a heating rate of 5-6°C/hr. followed by gradual heating up to 1100°C with the heating rate of 10-12°C/hr. and holding at that temperature for 2 hr., and (2) final sintering (no imbedding media): at 2100°C for 2 hr. in argon with the heating rate of 10- 12°C/hr.
- the final step was to heat the sample up to 1400°C in air to burn out graphite.
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Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52182798A JP2001504077A (en) | 1996-11-06 | 1997-11-05 | Multi-channel structure and manufacturing method thereof |
CA002309201A CA2309201A1 (en) | 1996-11-06 | 1997-11-05 | Multi-channel structures and processes for making such structures |
AU51065/98A AU5106598A (en) | 1996-11-06 | 1997-11-05 | Multi-channel structures and processes for making such structures |
EP97945635A EP0954399A4 (en) | 1996-11-06 | 1997-11-05 | Multi-channel structures and processes for making such structures |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/744,359 | 1996-11-06 | ||
US08/743,731 | 1996-11-06 | ||
US08/744,359 US5864743A (en) | 1996-11-06 | 1996-11-06 | Multi-channel structures and processes for making structures using carbon filler |
US08/743,731 US5774779A (en) | 1996-11-06 | 1996-11-06 | Multi-channel structures and processes for making such structures |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998019812A1 true WO1998019812A1 (en) | 1998-05-14 |
Family
ID=27114198
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1997/020418 WO1998019812A1 (en) | 1996-11-06 | 1997-11-05 | Multi-channel structures and processes for making such structures |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0954399A4 (en) |
JP (1) | JP2001504077A (en) |
AU (1) | AU5106598A (en) |
CA (1) | CA2309201A1 (en) |
WO (1) | WO1998019812A1 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2398797A (en) * | 2000-03-09 | 2004-09-01 | Smith International | Composite material |
DE102005023914A1 (en) * | 2005-05-24 | 2006-11-30 | Continental Aktiengesellschaft | Mold for vulcanizing tires comprises a profiled surface having air deviating paths consisting of micro-channels some of which are aligned perpendicular to the surface and extending from the surface to the rear surface |
WO2008028542A1 (en) * | 2006-09-08 | 2008-03-13 | Continental Aktiengesellschaft | Method of producing a vulcanizing mould with a number of profile segments that can be joined together to form a circumferentially closed mould, and vulcanizing mould |
WO2008064391A1 (en) | 2006-11-29 | 2008-06-05 | Steri-Flow Filtration Systems (Aust) Pty Ltd | An apparatus and method of producing porous membranes |
WO2013082066A1 (en) * | 2011-11-29 | 2013-06-06 | Corning Incorporated | Extruded body devices including sheet material hole masking |
CN114959287A (en) * | 2022-06-13 | 2022-08-30 | 赣州晨光稀土新材料有限公司 | Rare earth metal or rare earth alloy purification material, preparation method thereof and rare earth metal or rare earth alloy purification method |
CN115487604A (en) * | 2022-09-23 | 2022-12-20 | 东莞市名创传动科技有限公司 | Composite sintered filtering material |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
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JP4578324B2 (en) * | 2005-05-30 | 2010-11-10 | イソライト工業株式会社 | Method for producing porous ceramic molded body |
JP2008007342A (en) * | 2006-06-27 | 2008-01-17 | Toshiba Corp | Anisotropic porous ceramic material and method of manufacturing the same |
JP2009221055A (en) * | 2008-03-17 | 2009-10-01 | Toshiba Corp | Anisotropic porous material and membrane |
KR101873223B1 (en) * | 2016-02-25 | 2018-07-04 | 고려대학교 산학협력단 | System for manufacturing three-dimensional porous scaffolds and method for manufacturing initial feed rod |
KR101832262B1 (en) * | 2016-02-25 | 2018-02-27 | 고려대학교 산학협력단 | System and method for manufacturing three-dimensional porous scaffolds, and three-dimensional porous scaffolds manufactured thereby |
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1997
- 1997-11-05 JP JP52182798A patent/JP2001504077A/en active Pending
- 1997-11-05 EP EP97945635A patent/EP0954399A4/en not_active Withdrawn
- 1997-11-05 AU AU51065/98A patent/AU5106598A/en not_active Abandoned
- 1997-11-05 CA CA002309201A patent/CA2309201A1/en not_active Abandoned
- 1997-11-05 WO PCT/US1997/020418 patent/WO1998019812A1/en not_active Application Discontinuation
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US3790654A (en) * | 1971-11-09 | 1974-02-05 | Corning Glass Works | Extrusion method for forming thinwalled honeycomb structures |
US4772524A (en) * | 1986-04-14 | 1988-09-20 | The United States Of America As Represented By The Secretary Of Commerce | Fibrous monolithic ceramic and method for production |
US4818264A (en) * | 1987-04-30 | 1989-04-04 | The Dow Chemical Company | Multicapillary gas chromatography column |
US4965245A (en) * | 1987-07-17 | 1990-10-23 | Fujikura Ltd. | Method of producing oxide superconducting cables and coils using copper alloy filament precursors |
US5181549A (en) * | 1991-04-29 | 1993-01-26 | Dmk Tek, Inc. | Method for manufacturing porous articles |
Non-Patent Citations (1)
Title |
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2398797A (en) * | 2000-03-09 | 2004-09-01 | Smith International | Composite material |
GB2398797B (en) * | 2000-03-09 | 2004-10-13 | Smith International | Polycrystalline diamond carbide composites |
DE102005023914A1 (en) * | 2005-05-24 | 2006-11-30 | Continental Aktiengesellschaft | Mold for vulcanizing tires comprises a profiled surface having air deviating paths consisting of micro-channels some of which are aligned perpendicular to the surface and extending from the surface to the rear surface |
WO2008028542A1 (en) * | 2006-09-08 | 2008-03-13 | Continental Aktiengesellschaft | Method of producing a vulcanizing mould with a number of profile segments that can be joined together to form a circumferentially closed mould, and vulcanizing mould |
WO2008064391A1 (en) | 2006-11-29 | 2008-06-05 | Steri-Flow Filtration Systems (Aust) Pty Ltd | An apparatus and method of producing porous membranes |
AU2007327536B2 (en) * | 2006-11-29 | 2012-09-27 | Steri-Flow Filtration Systems (Aust) Pty Ltd | An apparatus and method of producing porous membranes |
WO2013082066A1 (en) * | 2011-11-29 | 2013-06-06 | Corning Incorporated | Extruded body devices including sheet material hole masking |
US9364814B2 (en) | 2011-11-29 | 2016-06-14 | Corning Incorporated | Extruded body devices including sheet material hole masking |
CN114959287A (en) * | 2022-06-13 | 2022-08-30 | 赣州晨光稀土新材料有限公司 | Rare earth metal or rare earth alloy purification material, preparation method thereof and rare earth metal or rare earth alloy purification method |
CN115487604A (en) * | 2022-09-23 | 2022-12-20 | 东莞市名创传动科技有限公司 | Composite sintered filtering material |
Also Published As
Publication number | Publication date |
---|---|
JP2001504077A (en) | 2001-03-27 |
EP0954399A4 (en) | 2003-06-04 |
AU5106598A (en) | 1998-05-29 |
EP0954399A1 (en) | 1999-11-10 |
CA2309201A1 (en) | 1998-05-14 |
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