AU628700B2 - Ceramic microspheres - Google Patents
Ceramic microspheres Download PDFInfo
- Publication number
- AU628700B2 AU628700B2 AU68472/90A AU6847290A AU628700B2 AU 628700 B2 AU628700 B2 AU 628700B2 AU 68472/90 A AU68472/90 A AU 68472/90A AU 6847290 A AU6847290 A AU 6847290A AU 628700 B2 AU628700 B2 AU 628700B2
- Authority
- AU
- Australia
- Prior art keywords
- microspheres
- range
- micrometers
- microsphere
- bauxite
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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- 239000004005 microsphere Substances 0.000 title claims description 133
- 239000000919 ceramic Substances 0.000 title description 44
- 239000002245 particle Substances 0.000 claims description 58
- 238000000034 method Methods 0.000 claims description 38
- 229910001570 bauxite Inorganic materials 0.000 claims description 37
- 239000002131 composite material Substances 0.000 claims description 37
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 32
- 239000011159 matrix material Substances 0.000 claims description 27
- 238000004519 manufacturing process Methods 0.000 claims description 25
- 238000001354 calcination Methods 0.000 claims description 20
- 238000005245 sintering Methods 0.000 claims description 20
- 239000013078 crystal Substances 0.000 claims description 19
- 239000011734 sodium Substances 0.000 claims description 17
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 13
- 239000006185 dispersion Substances 0.000 claims description 13
- 229910052708 sodium Inorganic materials 0.000 claims description 13
- 238000001694 spray drying Methods 0.000 claims description 13
- 229910052782 aluminium Inorganic materials 0.000 claims description 12
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 12
- 239000011707 mineral Substances 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 12
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 11
- 230000003014 reinforcing effect Effects 0.000 claims description 11
- 239000007787 solid Substances 0.000 claims description 11
- 229910052751 metal Inorganic materials 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 10
- 239000004411 aluminium Substances 0.000 claims description 9
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 claims description 9
- 229910052863 mullite Inorganic materials 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 9
- 239000004927 clay Substances 0.000 claims description 8
- 229910052593 corundum Inorganic materials 0.000 claims description 8
- 239000010431 corundum Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 238000004458 analytical method Methods 0.000 claims description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 125000002524 organometallic group Chemical group 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 238000001179 sorption measurement Methods 0.000 claims description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 2
- 239000011156 metal matrix composite Substances 0.000 description 35
- 229910045601 alloy Inorganic materials 0.000 description 21
- 239000000956 alloy Substances 0.000 description 21
- 239000012071 phase Substances 0.000 description 18
- 230000008569 process Effects 0.000 description 18
- 230000002787 reinforcement Effects 0.000 description 18
- 239000002002 slurry Substances 0.000 description 17
- 239000000463 material Substances 0.000 description 16
- 239000012779 reinforcing material Substances 0.000 description 14
- 239000000047 product Substances 0.000 description 13
- 238000007792 addition Methods 0.000 description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000005266 casting Methods 0.000 description 6
- 238000005755 formation reaction Methods 0.000 description 6
- 230000006872 improvement Effects 0.000 description 6
- 239000004033 plastic Substances 0.000 description 6
- 229920003023 plastic Polymers 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 6
- 229910000838 Al alloy Inorganic materials 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 239000011777 magnesium Substances 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000009736 wetting Methods 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 229910052622 kaolinite Inorganic materials 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000012798 spherical particle Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 229910001593 boehmite Inorganic materials 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000012767 functional filler Substances 0.000 description 3
- 229910001679 gibbsite Inorganic materials 0.000 description 3
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 229920000058 polyacrylate Polymers 0.000 description 3
- 238000004663 powder metallurgy Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 239000010936 titanium Substances 0.000 description 3
- 229910052719 titanium Inorganic materials 0.000 description 3
- 239000011882 ultra-fine particle Substances 0.000 description 3
- 238000009827 uniform distribution Methods 0.000 description 3
- 229910021364 Al-Si alloy Inorganic materials 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000000280 densification Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000000806 elastomer Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 238000001000 micrograph Methods 0.000 description 2
- 239000011236 particulate material Substances 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000005728 strengthening Methods 0.000 description 2
- 235000001674 Agaricus brunnescens Nutrition 0.000 description 1
- 229910001148 Al-Li alloy Inorganic materials 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical class Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 229910052810 boron oxide Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000010835 comparative analysis Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 210000003918 fraction a Anatomy 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 229910052595 hematite Inorganic materials 0.000 description 1
- 239000011019 hematite Substances 0.000 description 1
- 235000011167 hydrochloric acid Nutrition 0.000 description 1
- 238000010191 image analysis Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000001989 lithium alloy Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- UFMBFIIJKCBBHN-MEKJRKEKSA-N myelin peptide amide-16 Chemical compound C([C@@H](C(=O)N[C@@H](CC(C)C)C(=O)N[C@@H](C)C(=O)N[C@@H](CO)C(=O)N[C@@H](C)C(N)=O)NC(=O)[C@H](CCCCN)NC(=O)[C@H](CO)NC(=O)[C@H](CCCNC(N)=N)NC(=O)[C@H](CCC(N)=O)NC(=O)[C@H](CO)NC(=O)[C@H]1N(CCC1)C(=O)[C@H](CCCNC(N)=N)NC(=O)[C@H](CCCCN)NC(=O)[C@H](CCC(N)=O)NC(=O)[C@H](C)NC(=O)[C@H](C)NC(C)=O)C1=CC=C(O)C=C1 UFMBFIIJKCBBHN-MEKJRKEKSA-N 0.000 description 1
- 108010074682 myelin peptide amide-16 Proteins 0.000 description 1
- 229910021382 natural graphite Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- -1 oxides Chemical class 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 229920000307 polymer substrate Polymers 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004626 scanning electron microscopy Methods 0.000 description 1
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 1
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 1
- 235000019830 sodium polyphosphate Nutrition 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 238000009864 tensile test Methods 0.000 description 1
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 1
- 230000000930 thermomechanical effect Effects 0.000 description 1
- 230000009974 thixotropic effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 229910052845 zircon Inorganic materials 0.000 description 1
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
- E21B43/267—Methods for stimulating production by forming crevices or fractures reinforcing fractures by propping
-
- 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
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/10—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on aluminium oxide
- C04B35/111—Fine ceramics
-
- 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
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/16—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay
- C04B35/18—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay rich in aluminium oxide
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/60—Compositions for stimulating production by acting on the underground formation
- C09K8/80—Compositions for reinforcing fractures, e.g. compositions of proppants used to keep the fractures open
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Ceramic Engineering (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Structural Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacture Of Alloys Or Alloy Compounds (AREA)
Description
:I
~_II--L-YI~-_-L-LLLIliY I.(I-iiil.i. ~LL-~.III. :iiii..lii;l- 62870 COMPLETE SPECIFICATION FOR OFFICE USE Application Number: Lodged: Class: Int. Class: Complete Specification Lodged: Accepted: Published: Priority: Related Art: TO BE COMPLETED BY APPLICANT Name of Applicant: Address of Applicant: S Actual Inventor/s: Address for Service: COMALCO ALUMINIUM LIMITED 55 Collins Street, Melbourne, Victoria, 3000, Australia THOMAS KEITH SMITH RAYMOND WALTER SHAW CHRISTOPHER JOHN HEATHCOCK LESLIE CHARLES EDWARDS MALCOLM JAMES COUPER KENONG XIA SMITH SHELSTON BEADLE 207 Riversdale Road (P 0 Box 410) Hawthorn Victoria 3122 Australia (Attorney Code SA) Complete Specification for the invention entitled: CERAMIC MICROSPHERES The following statement is a full description of this invention, including the best method of performing it known to us: Page 1 Our Ref: #4891 TNB:CE 52.cal 2 TITLE: CERAMIC MICROSPHERES Field of the Invention: This invention is concerned with ceramic microspheres produced from bauxite and the use of such microspheres as reinforcing materials and functional fillers.
Background of the Invention: Various processes for the manufacture of microspheres of small diameter in the range 40-60 micrometers and with somewhat larger microspheres having a diameter in the range 0.25 to I t millimeters have been described in the prior art, for example Japanese Published Patent Application Number 57-84731 and *t4 United States Patent Number 4746468.
United States Patent Numbers 3491492, 4068718, 4427068 and 4713203 all describe processes for manufacture from clay or bauxite materials substantially spherical ceramic particles or t pellets in the size range 0.25-5.0 millimeters, primarily for use as proppants. Apart from United States Patent Number t4 S 4713203 which utilizes naturally occurring bauxite fines as feedstock the other prior art documents describe the use of relatively coarse clay or bauxite particles. United States S patent Number 4427068 does imply however that expensive grinding of calcined clays or bauxite may be employed to produce particle sizes less than 15 micrometers.
Each of United States Patents 3491492, 4068718, 4427068 and 4713203 is concerned with the manufacture of proppants for hydraulic fracturing of subterranean formations and each requires the physical formation of pellets by agglomeration in a rotary pelletizer or the like, with or without a binder.
Subsequently calcining of the green pellets is usually carried !tbspe.007/comalco 90 12 21 ii' i' 3out in a rotary calcining kiln.
Previous attempts to produce spherical proppants by spray drying have produced rounded non spherical particles characterized by a hollow recess similar in appearance to a xiushroom cap. This shape has been ascribed to aerodynamic deformation of the slurry droplet in the hot gas stream before the particle dried.
Metal-matrix composites (MMCs) consist of a matrix of a ft t S. metal or alloy into which one or more second phases have been I0.. incorporated with the aim of reinforcing for improved properties. After many years of research, these materials are f now becoming commercially available. The enhancement in
S
properties over those of the matrix material which can be achieved include: it improvement in strength at ambient and high temperatures, improvement in stiffness, improvement in fatigue strength, f S S- improvement in wear resistance, reduction in coefficient of thermal expansion.
2 These property enhancements have made MMCs attractive for structural applications at room temperature and at elevated temperatures. The magnitude of the enhaincements in properties depend on many factors, such as, the: matrix metal or alloy, content of the reinforcing phases, chemistry, geometry, distribution and orientation of the reinforcing phases, nature of the interface between the reinforcing phases and the matrix material, !tbspe.007/comalco 90 12 21 1 4 manufacturing method, thermo-mechanical history.
In addition, all other factors which generally affect properties of metallic materials, such as the heat-treatment, fabrication, porosity level, etc., also affect the properties of MMCs.
Aluminium, magnesium, titanium, copper and their alloys can be used as matrix materials. For reinforcing purposes, a r. variety of compounds such as carbides, oxides, nitrides, borides, etc. and elements such as carbon and boron, in various forms such as fibres, whiskers, platelets and particulates, 0.
Shave proven to be effective. High performance fibres and t* r whiskers are manufactured by costly, energy-intensive processes which make them expensive, resulting in high cost to the finished MMC product. There are certain lower performance i fibres and particulates, however, which produce moderate property improvements at low cost. The present invention
C
relates to a reinforcement for low-cost MMCs incorporating an *4 in inexpensive naturally occurring raw material.
Although, some naturally occuring materials such as natural graphite, mica aned zircon sand have been examined for reinforcing application in MMCs, they are not recommended because the properties of the resulting MMCs are generally poorer than those of the matrix. An important aspect of this invention is the use of a naturally occuring mineral as the starting material for reinforcement of MMCs and other composites leading to enhancement in properties.
The geometries of reinforcing materials employed by MMC producers are typically fibre, platelet and particulate. The !tbspe.007/comalco 90 12 21 _1II~- -1L_\Y LLI .IIIY1.. li _ll -F fibre geometry has a long dimension in one direction which is the preferred direction of reinforcement. Little or no reinforcing effect, sometimes even deleterious effects, are observed in the directions perpendicular to the longitudinal direction. The platelet geometry, in turn, imparts reinforcing effects only in the plane of the platelet which, again, is the preferred plane for reinforcement. Consequently, MMCs reinforced by fibres and platelets exhibit anisotropic r properties. Randomly oriented fibres and platelets can restore t* i0' isotropy but this is difficult to achieve in practice and a e* unlikely to be maintained during forming operations.
Particle reinforced composites do not exhibit the S.sotropic characteristics of fibre or platelet composites.
Hence they are the most efficient for the production of isotropic MMCs, in addition to being low in cost. The use of the ceramic microspheres defined above as a reinforcing material offers, by virtue of its geometry, a high degree of It isotropy to the MMCs.
The particulate materials presently used for reinforcing W" purposes have angular or irregular shapes. When reinforcements It t E, of such shapes are incorporated in a metallic matrix, the particles can act as stress raisers under the action of an applied stress. This can lead to premature nucleation of cracks with associated reduction in plasticity of the MMC. Reduced plasticity is reflected in lower elongation, toughness, formability and perhaps strength. The geometry and fine microstructure of the particulate material embodied in this invention is free of any stress raising features such that MMCs reinforced with the material have improved ability for plastic !tbspe.007/comalco 90 12 21 6 deformation.
Microspheres of the above type have now been determined to be suited for use as a reinforcement material in metals to form metal matrix composites as well as in other materials such as plastics, to provide improved strength and wearing properties. In making 4 microspheres for this purpose it is important to ensure that the microspheres have properties which promote "wetting" which determines the extent to which the interface of the microsphere transforms the strengthening effect of the ceramic.
Good wettability between the matrix alloy and the reinforcing material is critical for the production of good quality MMCs. Many studies have shown that commercial reinforcing materials are not easily wetted by molten metals and alloys, and similar comments apply S" with equal validity to offer materials such as t plastics. A good reinforcing material, therefore, should exhibit good wettability while being relatively inert to the matrix alloy. Such a reinforcing material is provided in this invention.
Summary of the Invention and Object: Accordingly, it is an aim of the present invention to provide bauxite microspheres having improved sphericity, density, such as chemistry and crystal structures and to provide a simple and economic method for the production of such microspheres from bauxite and bauxitic clays.
/According to one aspect of the invention there is tbcomalco.spe 92 5 4 ui~ 7 provided p calcined microspheres of ultrafine bauxite particles, suitable for use in reinforcing a matrix material, said microsphereShaving a particle size less than 100 micrometers and being characterised by a substantially solid form having a pycnometric density substantially falling in the range of 3.2 to 3.9 g/cm', a BET surface area substantially falling in the range of 0.05 to 0.5 m 2 /g and a crystal grain size of less than 4 micrometers, said microsphereshaving a surface chemistry that provides enhanced wettability of the microsphere to allow i-t-to mix with matrix materials and improved ability of the microsphere to bond strongly with the matrix materials.
In a preferred form of the invention, the miG-~ pharLare formed from bauxite particles having a mean particle size substantially falling within the range 0.01 to 0.3 micrometers and the microspheres have a particle size substantially falling in the range 1 to micrometers and most preferably less than micrometers and a crystal grain size of less than 2 S, micrometers.
By providing the calcined microsphereS with the i above defined properties, the microspheres are better adapted to perform well in the selected end composite.
All of the defined features influence wetting. Wetting in turn influences ease of preparation of the MMC and also determines how well the interface transfers the strengthening effect of the ceramic. The mechanical A properties (stiffness and strength) of the microsphere tbcomalco.spe 92 5 4
A
I
8 depend on the phases and structure which in turn influence properties of the composite product. The combination of spherical shape and microcrystalline structure provide isotropic properties in the composite.
The shape on its own influences certain properties since notch effects are eliminated and formability and castability are also improved.
The available range of microsphere size 0-100 um which is a consequence of the spray-drying method is an important advantage since other reinforcing materials are available in only limited size ranges. For example, commonly available SiC, A 2 0 3 have a narrow size range 1-5, 5-15, 10-25, etc.
Typical property data for a preferred calcined microsphere embodying the invention are SChemical Composition Wt% Al 2 0, 70 SiO, 4 Fe 2 0, 0 TiO, 0 6 Na 2 0 0.05 K,0 0 1 Phase Analysis Wt% Mullite 30 (3A10.. 2SiO, Corundum 10 (a Pseudobrookite 0 Al), TiO Crystal Grain Size less than 4 um Bulk (Tapped) Density 1.8 2.4g/cm' Pycnometric Density 3.2 3.9g/cm 3 tbcomalco.spe 92 5 4
LYL
9 BET Surface Area (Nitrogen Adsorption) Microsphere Particle Size Range 0.05- 0.5 m 2 /g 1 100 um less than 30 um According to another aspect of the invention there is provided a method for the manufacture of bauxite microspheres, comprising the steps of preparing a dispersion of bauxite or bauxitic clay; classifying the dispersed bauxite particles to recover the ultrafine fraction; adding small quantities of water soluble salts, mineral compositions or organometallic complexes to control the microsphere surface chemistry so as to enhance the wetting and dispersion of the microsphere and improve its ability to bonding strongly with the matrix materials in use; spray drying the dispersion to produce green microspheres of a predetermined mean particle diameter, and I II
III
r
III
0 subjecting said green microspheres to calcination and sintering to produce microspheres having a size within the range 0-100 micrometers, preferably from 1 to micrometers and most preferably less than micrometers, said microsphere being characterised by a substantially solid form having a pycnometric density substantially falling in the range 3.2 to 3.9 g/cm 3 a BET surface area substantially falling in the range 0.05 to 0.5 m 2 /g and a crystal grain size less than 4 micrometers.
In a preferred from of the, invention, between 0.05 tbcomalco.spe 92 5 4 9 and 5 wt% of the water soluble salt, mineral composition or organometallic complex is required to achieve the necessary modification of the surface chemistry of the resultant microsphere. The additions may contain elements selected from Group 1, 2 or 3 of the Periodic Table. Preferably sodium is present on the surface in a concentration of about 0.5 to 5 atomic weight percent.
Preferably said dispersion of bauxite or bauxitic clay comprises an aqueous slurry having a solids content in the range 10-70% w/w solids.
Suitably, spray drying is carried out by directing a fine spray of said slurry into a heated region under conditions adapted to produce green microspheres of predetermined mean particle size.
Preferably calcination and sintering is effected in a stationary or gas suspension calciner, in a temperature range t r tbcomalco.spe 92 5 4 I 10 between 1100°C and 1600°C, and most preferably between 1300°C and 1450°C.
According to yet another aspect of the invention there is provided a composite material comprising as a functional filler bauxite microsphere product in accordance with the invention.
Suitable composites include metalmatrix composites (MMCs) and plastics composites.
The present invention preferably uses ultrafine bauxite or bauxitic clay as the starting material. The relative ease of c I 1Q manufacture and the superior material properties of the product S formed from the preferred material arise primarily from the choice of starting material, an ultrafine fraction of a tct naturally occurring bauxite. This ultrafine fraction has a particle size typically less than 1 micrometer and more typically from about 0.02 to 0.3 micrometers with an associated So surface area of about 34 square metres per gram. This extreme fineness and the unique chemical composition of such ultrafine 0 bauxites lends advantages to the manufacturing process and resulting microsphere including: the need for expensive pregrinding is eliminated t C the need for expensive precalcin.tion is eliminated high strength of the green microspheres is obtained without the addition of a binder the very high surface area of the feed material makes it highly reactive. This leads to a reduction in sintering time, hence in energy consumption an exceptionally high degree of uniformity in the composition of the microspheres The advantages of the product produced according to the !tbspe.007/comalco 90 12 21 A 11 invention may be summarized as follows:- 1. The very fine particle size of the bauxite or bauxitic clay feedstock allows an exceptionally high degree of uniformity of blend in the manufacture of the green microsphere.
2. The green microsphere comprising a multitude of ultrafine particles has numerous points of contact between the particles, and it is at these points that sintering will be initiated.
t 3. It has been found that the extremely intimate dispersion of minerals and thus of constitutent elements is conducive to a high degree of reactivity within each microsphere as it Sis heated. This leads to a correspondingly intimate dispersion of microcrystallites on sintering. The microspheres thus exhibit very high strength. It is well 'f known in the art that ceramic products with a fine microcrystalline structure are extremely strong.
S4. The ultrafine particle size of the constituted minerals, combined with the small target size of the manufactured green microspheres, permits the use of the simple spray drying process to form particles of substantially spherical shape. Previous experience with the same material in spray drying to form larger particle diameters resulted in rounded but not spherical particles which were characterised by a shape of mushroom cap appearance. This shape has been ascribed to the aerodynamic deformation of the slurry droplet before it dried in the hot gas stream of the spray dryer. It has now been found that when the droplet size is restricted to a particle size less than about 100 micrometers, these deformities in shape !tbspe.007 /comalco 90 12 21 ii:li~~n -~ii i l~i-i ;i i 12 substantially disappear. Scanning electron microscopy reveals that sphericity of particles under about micrometers improves dramatically, with particles in the range from about 5 to 45 micrometers being almost perfectly spherical. It is believed that the higher rate of surface tension to mass in the fine droplets overcomes the tendency to form non-spherical particles.
Since the only mechanism employed in the formation of the green microspheres from the ultrafine particles is the removal of hygroscopic moisture by drying, it will be apparent that the optimum benefit has been obtained from Sr", the extremely high interparticulate Van der Walls's forces.
This leads to near maximum densification of the particles without the need for an expensive binder.
6. The spray drying process allows relatively simple control over the particle size of the green microspheres. Choice of such appropriate spray drying parameters such as slurry -i solids concentration, slurry viscosity rate of introduction of inlet and outlet temperature and spray head type and i tilt configuration permit this control to be achieved.
7. The choice of the calcination and sintering process is an important element in the large scale commercial production of ceramic microspheres from bauxite or bauxitic clay.
Although the small scale production by firing in loosely packed beds is feasible, the process must be interrupted at a relatively high temperature to allow the bed to be stirred and to prevent the particles sintering together at the temperature chosen for optimum densification of the individual particles. This is clearly not feasible on a !tbspe.007/comalco 90 12 21 13 commercial scale. The small size of the green microspheres and their free-flowing nature precludes the economic and practical use of conventional rotary kilns as unacceptable losses of finer microspheres would occur. It was considered that the use of modern stationary calciners such as the socalled flash and gas suspension calciners and which are successfully used for the calcination of such materials as fine aluminium trihydroxide would not be suitable for the calcination and sintering of the ceramic microspheres. It was thought that the very steep temperature gradient and tnt very short residence times typical of such apparatus would t lead to the shattering of the microspheres due to the inability of hygroscopic and chemically bound moisture to diffuse from the microspheres at sufficiently rapid rate.
I It was also thought that the turbulent nature of the hot gases in the calcination and sintering zone of the calciner S'that the microspheres would sinter together. Surprisingly, it was found that the amount of particle degradation in the product was low. It was also surprisingly found that few of the microspheres were sintered together.
a C f t In order that the invention may be more clearly understood reference is now made to preferred embodiments illustrated in the following examples and Figures in which: Figure 1 is a scanning electron micrograph of microspheres embodying the invention of size range 1 40 um; Figure 2 shows the microstructure of squeeze cast alloy 6061 15 vol% ceramic microspheres (mag. x 170); Figure 3 is a graph showing sliding wear resistance of unreinforced 6061 and 6061 reinforced with ceramic microspheres !tbspe.007/comalco 90 12 21 14 or SiC; Figure 4 shows the improved elevated temperature tensile strength of COMRAL-85 compared with unreinforced 6061; Figure 5 shows the improved fatigue strength of compared with unreinforced 6061; Figure 6 shows increased elevated temperature elastic modulus of COMRAL-85 compared with unreinforced 6061 (determined by the piezo-electric ultrasonic crystal oscillating technique PUCO); Figure 7 shows the stiffness of COMRAL composites as a function of volume fraction of ceramic microsphere S reinforcement; Figure 8 shows the density of COMRAL composites as a function of volume fraction of ceramic microshpere reinforcement; Figure 9 is an improved modulus-density combination of composites reinforced with ceramic microspheres compared with S pure A1 2 0 3 reinforcement; t a Figure 10 is a microstructure section of an extruded 2Q COMRAL-85 composite sample (unetched) showing the uniform distribution of particulate; Figure 11 is a further enlarged microstructure section of an extruded COMRAL-85 composite sample (unetched) showing the uniform distribution of particulate; Figure 12 is a microstructure action of a gravity cast Al-Si alloy reinforced with 15 vol% of ceramic microspheres (etched); Figure 13 is a further enlarged microstructure section of a gravity case Al-Si alloy reinforced with 15 vol% of ceramic !tbspe.007/comalco 90 12 21 S- 15 microspheres (etched); Figure 14 is a Bachscattered electron in:age of a ceramic microsphere in an aluminium matrix (polished section of an extrusion); Figure 15 is an image analysis of the shape of ceramic particulate in SiC reinforced composite compared with ceramic microsphere reinforced composite; Figure 16 is a low magnification scanning electron microscope (SEM) image of the calcined microspheres embodying the invention; Figure 17 is a high magnification scanning electron microscope (SEM) image of the calcined microspheres embodying the invention; Figure 18 shows the pin-on-disk sliding wear resistance of COMRAL-85 compared with unreinforced 6061, and Figure 19 compares the fatigue of COMRAL-85 and a S commercial A1 2 0 3 reinforced composite and unreinforced 6061.
Finely divided materials suitable for the production of ceramic microspheres according to the invention are readily 2 obtained from bauxite deposits such as for example those of the type occurring at Weipa in Northern Queensland. In these and similar bauxites and bauxitic clays, a. fine fraction exists which is easily separated, for example, by slurrying the bauxite in water in the presence of a dispersant. A variety of dispersants may be used, such as compounds based on phosphates or polyacrylates.
A simple separation step results in recovery of the fine fraction as a dilute slurry from coarse particulate matter.
Satisfactory separation may be effected for instance using !tbspe.007/comalco 90 12 21 i L .'?il"T~iliiji~~iiiillLll.(iii ii I~riii~ -I L(- 16 gravity settlers or hydrocyclones.
In order to render the process economical it is necessary to increase the solids concentration of the slurry of fine particles. This may be conveniently done by adjusting t; pH of the slurry to about pH7 by the addition of acid. Sulphuric and hydrochloric acids are satisfactory for this purpose. The fine particles are then seen to agglomerate. These agglomerates are then observed to settle. It will be recognised by those skilled in the art that flocculants may be used to assist in the more rapid settling and increasing the Sdensity of the settled solids.
The solids content of the settled slurry may still be too low for economical operation of the process, and it may be necessary to introduce a further dewatering step, such as centrifugation or filtration.
The thickened solids now have the consistency of a paste, and it is necessary to redisperse them to a suitably low viscosity before the next step.
More efficient dispersion may be facilitated by the addition of dispersants such as polyacrylates e.g. ammonium polyacrylate, sodium hexametaphosphate or sodium polyphosphate.
The use of a high intensity mixer aids in the destruction of agglomerates and the dispersion of most of the particles in their liberated form.
A spray dryer, such as manufactured by the Niro company, or as manufactured by the Bowen-Stork company, is used to form the green microspheres. It is possible to exercise control over particle size distribution by controlling the preparation of the dispersed slurry and the conditions of operation of the !tbspe.007/comalco 90 12 21 1 17 spray dryer.
It has been found that the particular fraction of bauxite proposed as a source of microspheres has in the Weipa deposits an alumina content of about 59% with a typical range from 63%. Similarly, the silica content will average about with a range typically 7-13%. Substantially, all of this silica will be present as the mineral kaolinite, although small amounts of quartz may be present. Typically, the mineralogy will comprise 30-50% gibbsite with 15-45% boehmite, 16-27% kaolinite with less than 0.2% quartz. Oxides of iron 6-10% and S titanium 3-5% will total about 8-14%. This relatively high level of iron oxide reduces the calcination temperature and results in the formation of the pseudobrookite phase in the calcined microspheres.
i 15, Electron microscope studies have confirmed that the mineral S, particles are typi ly from about 0.02 to 0.3 micrometers in diameter and the minerals gibbsite, boehmite,kaolinite, hematite and anatase are commonly present as liberated crystallites. In other words, the particles are frequently mono-minerallic in nature, and because of the large surface area and the presence of relatively high levels of non-oxide in the bauxite chemistry, rapid reaction between particles is facilitated at elevated temperatures, producing mainly corundum and mullite.
In the course of heating such a product to the typical range of 13000 1600°C to produce the range of properties typically required in the product, a series of changes occurs in the microspheres.
The alumina minerals which are present, namely, gibbsite, !tbspe.007/comalco 90 12 21 li:i 18 boehmite and kaolinite progressively lose their combined water as the temperature is increased to about 600"C.
The crystal lattices become disordered and as the temperature is further increased the aluminium oxides undergo a series of phase changes. It is to be expected that the sequence of phase changes may include as transition states gamma, delta, theta, chi and kappa forms of alumina. As a temperature of approximately 950 0 C the formation of mullite V, commences and at about 1050'C the alumina begins to convert to t t 1Oi" the alpha-phase mineral which is known as corundum. Further ti st ,Q increase in temperature causes sintering of the mullite and corundum and the production of a pseudobrookite phase to form a polycrystalline ceramic body with high strength. The phases corundum, mullite and pseudobrookite are the final major phases in the end product. As the temperature is increased the particles gain in compressive strength due to the development of an extremely fine interlocking network of crystals.
,r tt Excessively high temperatures result in a coarsening of the crystal size which then reduces the strength of the ceramic.
During sintering, the pellets may shrink in diameter by up to 30% so the spray drying process is controlled to produce green microspheres which will produce the required calcined microsphere falling in the preferred ranges 1-100 micrometers, and preferably less than 30 micrometers.
The high reactivity of the uncalcined bauxite and its very fine particle size facilitates the formation of the required phases.
The green microspheres are subjected to calcination and sintering to form the final product. On a laboratory scale, !tbspe.007/comalco 90 12 21 19 calcination is performed by placing the green microspheres in a suitable crucible and heating the crucible in a muffle furnace to about 900°C. The heating rate should be slow enough to allow diffusion of the chemically bonded water to occur. This rate is suitable of the order of about 100 0 C/hour.
After the initial temperature range of about 900°C has been attained, heating is continued with a temperature increase rate of about 10°C/minute until the crucible and its contents reach about 1300°C. The process is then interrupted to prevent the sintering of the particles to each other.
o The material is cooled, lightly crushed to break up any agglomerates and screened through a 106 um screen to ensure individual particles. The microspheres are then returned to o 0.
the crucible and rapidly fired up to the final sintering temperature of between 1300°C-1600°C at a rate of about It is apparent to those skilled in the art that the temperatures and times chosen for the sintering of the o microspheres are dependent on the chemical composition of the 1 4 0 Q 0 raw material, as well as the desired properties of the product.
For instance, density and porosity of the product may be varied by altering the sintering temperature and time.
Generally, a sintering temperature between 1300°C and 1600°C is used.
The economic production of ceramic microspheres on a largescale industrial basis demands a continuous calcination process, rather than the batch process previously described.
This is most satisfactorily accomplished in a stationary gas suspension calciner, in which the particles are transported by a moving stream of gas through the drying, calcination and tbsp 07/cmalc 90 2 2 !tbspe-007/comalco 90 12 21 it 20 cooling sections of the apparatLu. The product may be separated by gravity, or by cycloning or filtration.
For purposes of example, such devices are manufactured by the Dentsche-Babcock and Lurgi companies of the Federal Republic of Germany, the F.L. Smidth company of Denmark, or the Fuller company of the United States of America. As well as being a more economic process, improvements to the quality of the product are noted. This is particularly in respect to the microcrystallinity of the particles which is expressed in the surface and strength of the sintered particles.
Gas suspension calciners feature a particularly short t. residence time of particles in the sintering zone of the furnace. For instance, the High Temperature Mixer manufactured a I I tl' by the Beutsche Babcock company, features a residence time in the calcination zone estimated at about one quarter to one half of a second. As a consequence of this short residence time, crystal grain growth is inhibited, and a fine crystal S microstructure is evident. The average crystal grain size has been estimated to be about one micrometer. As is known to those skilled in the art, a fine microstructure is conducive to obtaining strength in a ceramic object. The fine microstructure is also important in conveying a smooth surface t t "a to the microspheres. When used in composites which are to be subject to such processes as injection moulding, wear of the surfaces of the forming equipment is reduced.
Using the process described above, the following bauxite microspheres were produced !tbspe.007/comalco 90 12 21 21 Example 1: Chemical Analysis Al 203 S1i02 Fe 2 0 3 T1O 2 Na 2
O
Wt 73.0 13.7 4.3 0.15 Wt% Phase Analysis Mullite Corundum Pseudobrookite Crystal grain size Bulk (Tapped) Density Pycnometric Density BET Surface Area 0. 2 2 umn 2. 1 g/cm 3 3.66 g/cm 3 0.14 M 2 /g q2 9 4 445, .49.
*4 05 r itt' Particle Size Distribution (Leeds Particle Diameter (urn) 11 7.8 3.9 and Northrup Microtrac) Cummulative Percent Passing 100 92.4 64.6 32.4 13.3 1.7 0.3 0 Wt% 71.6 17.2 7.02 3.82 0.13 wt/ 0 23 0.3 1 urn Example 2: Chemical Analysis A 1203 2 Fe 2 0 3 2 Na 2
O
Phase Analysis Mullite Corundum Pseudobrookite Crystal grain size Bulk (Tapped) Density Pycnometric Density BET Surface Area 2. 0 g/cm 3 3.42 g/cm 3 0.12 M 2 /g !tbspe .007/coilalco 9 22 90 12 21 22 Particle Size Distribution (Malvern Mastersizer) Cummulative Percent Passing 100 100 60 92 56 27 8 5 3 2 1 3.9 0 The sodium levels in the samples described in Examples 1 and 2 were carefully controlled by the addition of 0.15 wt/wt% sodium hydroxide during the slurry preparation step. The sodium was added to modify the surface composition of the microsphere for certain applications such as the reinforcement of aluminium alloys. The presence of sodium on the particle surface enhances wetting and dispersion. The surface enrichment of sodium occurs I2'G' during the spray drying process from the crystallization of dissolved sodium hydroxide at the microsphere particle surface.
X-ray photoelectron spectroscopy (XPS) studies confirmed this and results are given for sodium enrichment on the surface of ti the sample described in Example 2.
Atomic Weight Surface Sodium Concentration 0.2 (outer 10 Angstrom layer) I Without Sodium Addition SSurface Sodium Concentration 1.9 With Sodium Addition Surface Sodium Concentration of above Sample after removal of outer 100 Angstrom layer (100 x 10- 1 m) In the case of a plastics matrix, the desired surface chemistry can be achieved with the addition of water soluble inorganic compounds such as boron oxide or boric acid prior to !tbspe.007/comalco 90 12 21 :i I 4 23 spray drying. Small additions (0.1-5 wt%) during slurry preparation will result in a boron enriched surface layer during spray drying. This will assist with microsphere wettability and dispersion in a plastic or polymer matrix.
Bauxite microspheres produced in accordance with the invention may be used for a variety of purposes and in particular may be used as functional fillers in a variety of media. The ceramic composition of the particles lend such properties as toughness, hardness, wear and abrasion resistance, chemical resistance, resistance to weathering and the like in a composite material. The surface characteristics of the microspheres may also be modified, due to crystal structure (Figs. 14 and 17), by controlling the calcination conditions.
The microspheres embodying the invention are particularly adapted for use for reinforcement of metals and polymers and plastics. In general, aluminium, magnesium, copper, nickel or titanium, or their alloys could be used as the matrix material, f t but aluminium and its alloys are preferred. New aluminium alloys such as Al-Li alloys also can be used besides the conventional casting and wrought alloys.
Processes presently employed to produce MMCs can be used to t L 1 produce the novel MMC disclosed above. In particular, a foundry-based method of assimilating the reinforcing material in molten metal is the most desirable for the production of low cost MMCs. A foundry-based method is therefore proposed as the preferred production method, although other methods such as those based on powder metalurgy techniques and preform infiltration also can be used. A foundry-based method is !tbspe.007/comalco 90 12 2i 24 particularly suitable, because the ceramic microspheres are easily wetted by molten aluminium compared with other types of reinforcement. Furthermore, the sphericity of the reinforcing material results in increased fluidity and castability of the composite melt when compressed with other MMC melts.
Consequently, production and casting of this novel composite is easier via a foundry-based method than for other MMCs.
Porous preforms could be also made with microsphere particles. These could be infiltrated by a molten alloy by use of pressure or vacuum to produce MMC billets or near net shape castings.
*f The wettability between microspheres and aluminium alloys c,,r is promoted by the chemical and phase composition of the ceramic microspheres as well as by the surface chemistry 1. described above. The mineral forms present in the ceramic microspheres, in particular pseudobrookite and mullite, appear to be wet by molten metals better than pure aluminium oxide while still being resistant to them. The natural balance between the various chemical components in the microspheres thus provides the dual characteristics of good wettability and chemical inertness with respect to the matrix a feature which is not achieved by any other reinforcing material known to us.
I The spherical shape is geometrically the most isotropic shape. Furthermore, unlike other reinforcing materials, the calcined bauxite microspheres are polycrystalline which eliminates even crystallographic anisotropy which is inherent in single crystal whiskers, platelet, and particulates.
Therefore, the novel spherical bauxite particulates described above have the highest degree of isotropy among all available !tbspe.007/comalco 90 12 21 I 25 reinforcing materials. This fact, combined with uniform distribution in the matrix, will endow MMCs with maximum Iisotropy.
J The content of thiie microsphere reinforcing material in an S 5 MMC can be varied from 1 vol% to as high as 50 vol% but, when a foundry-based production method is used, practical difficulties K inmixing and casting generally limit the reinforcement content to levels below 30 vol%. When a powder metallurgy production I method is employed, however, this upper limit could be as high 10 as 50 vol%. The lower limit for reinforcement content is determined by the resulting properties. To achieve noticeable I enahancements in properties, a reinforcement content of at flit least 5 vol% must be present.
j' Methods of preparing metal matrix composites using the 5 preferred microspheres are described below: Example 3: 1 Alloy 6061 15 vol% Cera ic Microspheres Produced by Melt L Stirring This example describes a metal matrix composite where the 2 commercial aluminium alloy 6061 was reinforced by ceramic microspheres. A foundry-based method of preparation was used.
Approximately 3.5kg of aluminium alloy 6061 was melted in a S crucible. A quantity of ceramic microspheres was weighed out so as to produce an MMC with reinforcement content of 15 vol%.
this measured quantity was preheated to 200°C in an oven. The size of the microspheres of bauxite varied between about 1 um and 40 um. A scanning electron micrograph of these particles is shown in Figure 1, which demonstrates their sphericity and polycrystallinity.
!tbspe.007/comalco 90 12 21 26 The molten alloy was then stirred by a rotor at 700 0 C in order to produce a vortex on the melt surface. Hot ceramic microsphere particulates were then added into the vortex. After adding the particulates, stirring :as stopped and the molten composite was squeeze cast into blocks of iiOmm x 60mm x Specimens were machined from these blocks for testing.
A typical microstructure of the composite is shown in Figure 2. It demonstrates that the particles are individually wetted. The room temperature tensile test results after a T6 heat treatment are given in Table 1. Results are given for a A, A 2 0 3 reinforced 6061, produced via a foundry process by a commercial manufacturer, for comparison. The data show that the microsphere reinforced MMC exhibits higher yield strength than the corresponding commercial MMC while being comparable in other properties.
Results of the pin-on-disc wear tests are given in Figure 3. The microsphere reinforced MMC exhibits wear resistance comparable with SiC reinforced MMCs.
Example 4: Alloy 6061 10 vol% Ceramic Microspheres by Compocasting Approximately 3.5kg of commercial aluminium -lloy 6061 was melted in a crucible and 10 vol% ceramic microspheres were preheated as in Example 1.
When the alloy was molten, 0.3 wt% Mg was added to the alloy to compensate for Mg lost in the production process. The metal was then stirred at low speeds (120-150 rpm) by a multiblade stirrer so that a vortex did not form. The uppermost blades of the stirrer were level with the liquid surface.
The melt was cooled to the two-phase region while stirring !tbspe.007/comalco 90 12 21 r X: i 27 to a thixotropic slurry. When a temperature of 645°C was reached, the preheated ceramic microspheres were added at a slow and steady rate. The uppermost blades assimilated the bauxite into the slurry while sweeping its surface. After the completion of bauxite addition, stirring was continue in the temperature range 605°C 645 0 C until all the bauxite was wetted and distributed in the liquid phase of the slurry.
The material was then reheated to 700"C while being stirred to remelt the whole slurry. It was cast into a 5 inch diameter billet and extruded into 25mm diameter bars. The room temperature properties evaluated in the extruded bar after heat treatment as in Example 1 are given in Table 1.
Example Alloy 6061 10 vol% Ceramic Microspheres by Powder Metallurgy 11 Powders of Al (-325 mesh), Mg (-325 mesh) and Si (-20 um) were weighed out in a ratio to comply with the specification for alloy 6061 and to make a total weight of approximately 7kg.
The powders were mixed with 10 vol% ceramic microspheres and S were milled in an inert atmosphere for about 15 minutes.
2 0 The blended powder was filled and vibrated into an elastomer mould of diameter 89mm (3.5 inch) and length 430mm (17 inch). The mould was vacuum sealed and cold-isostatically pressed. The elastomer mould was then stripped and the cold pressed billet was sintered to produce a 95% dense billet.
The sintered billet was extruded into 12.5mm (0.5 inch) diameter bar and room temperature mechanical properties were determined (Table 1) after the heat treatment as in Examples 1 and 2.
!tbspe.007/comalco 90 12 21 28 TABLE 1 MECHANICAL PROPERTIES OF 6061-BASED BAUXITE COMPOSITES AFTER T6 HEAT TREATMENT tt a2 t t *4 *1 atr a a a Material Production Yield Modulus Method Stress (GPa) (MPa) 6061+15 vol% Melt stirred 328 86.6 Ceramic Microspheres and squeeze cast 6061+10 vol% Compocast 300 78.3 Ceramic Microspheres and extruded 6061+10 vol% Powder metallurgy 320 78 Ceramic Microspheres CIPPED, sintered and extruded 6061+0.5Mg+19V/O Cast and extruded 305 88 CMS (-30 urn) (Standard T6) "t 330 88 (New T6) PM 6061+19V/O Sintered and 327 88 CMS (-100 um) extruded (Standard T6) Duralcan 6061+10 vol% Melt stirred 296 81 ALO0 3 and extruded From Duralcan data sheets.* 1. 1.5h/530°C 20h/RT pre age, age 8h/175°C 2. 1.5h/530 C, direct age 6h/160°C Further composites formed using microspheres embodying the present invention are further disclosed in the following example: Example 6: Description Comral-85 is an aluminum matrix, up to Matrix Reinforcement v/o, ceramic microsphere reinforced composite.
Standard alloy 6061 Alumina containing microspheres: type with an average particle size of 20 microns.
!tbspe.007/comalco 90 12 21 a llc--Y- 29 Designation 6061/A1203/20p (proposed Aluminum Association) Tensile Properties of 19 mm Bar: As Extruded Properties: Dynamic Ultimate Young's (0.2%)Yield Tensile Modulus/(min) Strength Strength Elongation 105 MPa 200 MPa 16% Heat Treated Properties Dynamic Ultimate Young's (0.2%)Yield Tensile Modulus/(min) Strength Strength Elongation GPa 305 MPa 330 MPa 3.4% 12.3 Msi 44.2 ksi 47.9 ksi 3.4% L[ in the "T6" conditions 1.5 hrs 530°C; age 8 hrs 175°C.
Conventional 6061 (for comparison) 69 GPa 276 MPa 310 MPa 17% Msi 40 ksi 45 ksi 17% Fatigue and elevated temperature properties are shown in Figures 4,5 and 6 while the room temperature stiffness and S density properties are shown in Figures 7, 8 and 9. Micrographs tr S of the composite and an alternative composite (Comral 80) are Sshown in Figures 10 to 14. Comral-80 is a composite with matrix 's 601 (a casting alloy). A comparative analysis of a commercial composite and a composi-, embodying the invention is provided in Figure 15 and shows the significantly higher percentage of more spherical particles provided by the microspheres embodying the invention and Figures 16 and 17 are micrographs of the microspheres from which their sphericity and fine crystal structure is self-evident. The excellent wear resistance of is evident from Fig. 18. The excellent fatigue resistance of COMRAL-85 is compared with a commercial composite !tbspe.007/comalco 90 12 21 j iil- lil-__ 1.X l lf l I. 30 and the unreinforced 6061 in Figure 19.
Composites, such as the above example, embodying the invention can be heat treated to achieve strengths higher than those quoted in Example 6.
Example 7: Various ceramic microsphere reinforced composites were prepared by casting and extrusion of 5" billets into 19 mm rod.
A range of volume fractions of particulate and various particulate size ranges were used. Evaluation of the tensile properties in (Table 3) indicate that the best combination of r tensile strength and ductility is achieved with cermic particulate of size less than 30 um.
Example 8: Various ceramic microsphere reinforced composites were prepared by adding 10 vol% of particulate to alloy 6061. The final calcination temperature for preparation of the microspheres was varied. Excellent tensile properties are obtained (Table particularly for microspheres with a final calcination temperature in the range of 1400°C 1450°C.
!tbspe.007/comalco 90 12 21 31 TABLE 2 Room temperature tensile properties of T6 heat-treated extrusions for various microsphere reinforced 6061-based composites Nominal Reinforcement No. of Rp 2 A No. of Vol. Size Batches (MPa) (MPa) Tests Fraction A 15 0-100 um 2 304 326 2.4 8 B 0-45 um 3 302 322 3.4 14 C 0-30 um 1 301 328 4.0 12 D 19 0-30 um 4 316 344 3.7 23 E 24 0-45 um 1 330 345 0.7 4 TABLE 3 Typical tensile properties for 6061+0.3Mg 10 vol% CMS (T6 temper) with different CMS microstructures Sintering S.A. L.F.D. Rpo.
2 R, E A 5 No. of condition (m 2 (g/cm 3 (MPa) (MPa) (GPa) tests 1350°C/3hrs 1.01 1.46 1400°C/lhr 0.18 1.55 14000C/3hrs 0.13 1.50 298 315 81.0 3.2 2 1450,C/lhr 0.12 1.52 309 332 5.7 2 1450oC/3hrs 0.19 1.47 301 318 81.8 1.9 2 1480 0 C/3hrs 0.20 1.37 302 313 81.0 1.4 2 6061+0.3Mg 266 295 68.3+ 19.5 3 io I t l Extensive reaction was observed, S" From Metals Handbook S.A. surface area of CMS L.F.D. loose fill density of CMS Ro.2 0.2% proof stress R, ultimate tensile stress E Young's modulus
A
5 tensile elongation no test conducted The entire contents of the provisional specification lodged with Australian Patent Application of which this is the !tbspe.007/comalco 90 12 21 32 complete specification is hereby imported into this specification and forms part of the disclosure of this specification. The claims form part of the disclosure of this specification.
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Claims (13)
1. A eeleincdL microsphereS of ultrafine bauxite particles, suitable for use in reinforcing a matrix material, said microsphereShaving a particle size less than 100 micrometers and being characterised by a substantially solid form having a pycnometric density substantially falling in the range of 3.2 to 3.9 g/cm, a BET surface area substantially falling in the range of 0.05 to 0.5 m'/g and a crystal grain size of less than 4 micrometers, said microsphereShaving a surface chemistry that provides enhanced wettability of the microsphere to allow -i4- to mix with matrix materials and improved ability of the microsphereS to bond strongly with the matrix materials.
2. The microspheres of claim 1, formed from bauxite S; particles having a mean particle size substantially falling in the range 0.01 to 0.3 micrometers.
3. The microspheresof claim 1 or 2, having a particle o, size substantially falling in the range 1 to micrometers.
4. The microsphereSof claim 1 or 2, having a particle size less than 30 micrometers.
5. The microsphere5of any one of claims 1 to 4, having properties falling substantially within the following ranges: Chemical Composition Wt% A120, 70 SiO, 4 Fe,0 3 0 Ti02 0 6 'Na,0 0.05 SK0 0 1 tbcomalco.spe 92 5 4 r 3, C 34 Phase Analysis Mullite (3A1 2 0 3 .2SiO 2 Corundum (a A1 2 0,) Pseudobrookite Al) 2 Ti0,] Crystal Grain Size Bulk (Tapped) Density Pycnometric Density BET Surface Area (Nitrogen Adsorption) Microsphere Particle Size Range wt% 30 10 0 Less than 4 um 1.8 2.4g/cm 3 3.2 3.9g/cm 3 0.05- 0.5 m 2 /g 1 100 um
6. The microsphere5 of any preceding claim, wherein said surface chemistry is characterised by a surface rich in sodium.
7. The microsphereS of claim 6, wherein the surface sodium concentration substantially falls within the range of 0.5 to 5 atomic weight percent.
8. A method for the manufacture of bauxite microspheres, comprising the steps of preparing a dispersion of bauxite or bauxitic clay; classifying the dispersed bauxite particles to recover the ultrafine fraction; adding small quantities of water soluble salts, mineral compositions or organometallic complexes to control the microsphere surface chemistry to provide enhanced wettability and therefore dispersion of the microsphereSand improved ability of the microsphere to i, bond strongly with the matrix materials; 2 3 7.~ ,ii *t I^ tbcomalco.spe 92 5 4 k-- 35 spray drying the dispersion to produce green microspheres of a predetermined mean particle diameter, and subjecting said green microspheres to calcination and sintering to produce microspheres having a size less than 100 micrometers, said microsphere being characterised by a substantially solid form having a pycnometric density substantially falling in the range 3.2 to 3.9 g/cm 3 a BET surface area substantially falling in the range 0.05 to 0.5 m 2 /g and a crystal grain size less than 4 micrometers.
9. The method of claim 8, wherein calcination is carried out at a temperature which produces a sufficiently high density and a crystal grain size not exceeding 4 micrometers.
10. The method of claim 9, wherein calcination is 4 carried out substantially within the temperature range carried out substantially within the temperature range 1300 0 C to 14500C. I 'I
12. The method of any one of claims 8 to 11 l i substantially as described with reference to the Examples.
13. Calcined microspheres when produced by the method of any one of claims 8 to 12.
14. A composite material comprising a metal or polymer matrix reinforced by calcined microspheres as claimed in i any one of claims 1 to 7 or 13. tbcomalco.spe 92 5 4 rrsms~ 36 A composite comprising aluminium and calcined microspheres as claimed in any one of claims 1 to 7 or 13. DATED this 4 May 1992 CARTER SMITH BEADLE Fellows Institute of Patent Attorneys of Australia Patent Attorneys for the Applicant: COMALCO ALUMINIUM LIMITED Ile 4; tbcomalco.spe 92 5 4
Priority Applications (1)
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AU68472/90A AU628700B2 (en) | 1989-12-22 | 1990-12-21 | Ceramic microspheres |
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AUPJ8009 | 1989-12-22 | ||
AUPJ800989 | 1989-12-22 | ||
AUPK0045 | 1990-05-09 | ||
AUPK004590 | 1990-05-09 | ||
AU68472/90A AU628700B2 (en) | 1989-12-22 | 1990-12-21 | Ceramic microspheres |
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AU6847290A AU6847290A (en) | 1991-06-27 |
AU628700B2 true AU628700B2 (en) | 1992-09-17 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008092516A1 (en) * | 2007-01-30 | 2008-08-07 | Evonik Röhm Gmbh | Molding compound for matt molded polyacrylate bodies |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU521930B2 (en) * | 1978-06-12 | 1982-05-06 | Norton Co. | Proppants |
GB2092561A (en) * | 1978-12-13 | 1982-08-18 | Kennecott Corp | Sintered high density spherical ceramic pellets |
US4623630A (en) * | 1982-02-09 | 1986-11-18 | Standard Oil Proppants Company | Use of uncalcined/partially calcined ingredients in the manufacture of sintered pellets useful for gas and oil well proppants |
-
1990
- 1990-12-21 AU AU68472/90A patent/AU628700B2/en not_active Ceased
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU521930B2 (en) * | 1978-06-12 | 1982-05-06 | Norton Co. | Proppants |
GB2092561A (en) * | 1978-12-13 | 1982-08-18 | Kennecott Corp | Sintered high density spherical ceramic pellets |
US4623630A (en) * | 1982-02-09 | 1986-11-18 | Standard Oil Proppants Company | Use of uncalcined/partially calcined ingredients in the manufacture of sintered pellets useful for gas and oil well proppants |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008092516A1 (en) * | 2007-01-30 | 2008-08-07 | Evonik Röhm Gmbh | Molding compound for matt molded polyacrylate bodies |
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AU6847290A (en) | 1991-06-27 |
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