US20050234136A1 - Colloidal compositions and methods of preparing same - Google Patents
Colloidal compositions and methods of preparing same Download PDFInfo
- Publication number
- US20050234136A1 US20050234136A1 US10/827,214 US82721404A US2005234136A1 US 20050234136 A1 US20050234136 A1 US 20050234136A1 US 82721404 A US82721404 A US 82721404A US 2005234136 A1 US2005234136 A1 US 2005234136A1
- Authority
- US
- United States
- Prior art keywords
- metal
- silicate
- solution
- colloidal
- silica
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 238000000034 method Methods 0.000 title claims abstract description 59
- 239000000203 mixture Substances 0.000 title claims abstract description 58
- 229910052751 metal Inorganic materials 0.000 claims abstract description 134
- 239000002184 metal Substances 0.000 claims abstract description 134
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000003381 stabilizer Substances 0.000 claims abstract description 35
- 239000000243 solution Substances 0.000 claims description 157
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 135
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 78
- 235000012239 silicon dioxide Nutrition 0.000 claims description 77
- 239000000084 colloidal system Substances 0.000 claims description 65
- 239000002245 particle Substances 0.000 claims description 59
- 239000000377 silicon dioxide Substances 0.000 claims description 53
- 229910052914 metal silicate Inorganic materials 0.000 claims description 46
- 239000012670 alkaline solution Substances 0.000 claims description 22
- 150000001412 amines Chemical group 0.000 claims description 12
- 229910052723 transition metal Inorganic materials 0.000 claims description 11
- 150000003624 transition metals Chemical class 0.000 claims description 11
- 150000001875 compounds Chemical class 0.000 claims description 8
- -1 wave guides Substances 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- 229910052783 alkali metal Inorganic materials 0.000 claims description 6
- 150000001340 alkali metals Chemical class 0.000 claims description 6
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 6
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 6
- 229910052747 lanthanoid Inorganic materials 0.000 claims description 6
- 150000002602 lanthanoids Chemical class 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 5
- 239000010457 zeolite Substances 0.000 claims description 5
- 229910021536 Zeolite Inorganic materials 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 229910052755 nonmetal Inorganic materials 0.000 claims description 4
- 238000005498 polishing Methods 0.000 claims description 4
- 239000003082 abrasive agent Substances 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 3
- 230000014759 maintenance of location Effects 0.000 claims description 3
- 239000004065 semiconductor Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 239000011230 binding agent Substances 0.000 claims description 2
- 229910010293 ceramic material Inorganic materials 0.000 claims description 2
- 238000005352 clarification Methods 0.000 claims description 2
- 238000000576 coating method Methods 0.000 claims description 2
- 239000002537 cosmetic Substances 0.000 claims description 2
- 238000002425 crystallisation Methods 0.000 claims description 2
- 230000008025 crystallization Effects 0.000 claims description 2
- 238000009472 formulation Methods 0.000 claims description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims description 2
- 238000005495 investment casting Methods 0.000 claims description 2
- 239000012528 membrane Substances 0.000 claims description 2
- 239000002808 molecular sieve Substances 0.000 claims description 2
- 239000004038 photonic crystal Substances 0.000 claims description 2
- 102000004169 proteins and genes Human genes 0.000 claims description 2
- 108090000623 proteins and genes Proteins 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 2
- 238000011068 loading method Methods 0.000 abstract description 6
- 239000006185 dispersion Substances 0.000 abstract description 4
- 125000003277 amino group Chemical group 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 27
- 230000015572 biosynthetic process Effects 0.000 description 23
- 229910052782 aluminium Inorganic materials 0.000 description 20
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 20
- 239000010410 layer Substances 0.000 description 20
- 238000003786 synthesis reaction Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 239000007790 solid phase Substances 0.000 description 15
- JGDITNMASUZKPW-UHFFFAOYSA-K aluminium trichloride hexahydrate Chemical compound O.O.O.O.O.O.Cl[Al](Cl)Cl JGDITNMASUZKPW-UHFFFAOYSA-K 0.000 description 11
- 229910052684 Cerium Inorganic materials 0.000 description 10
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 description 10
- WGTYBPLFGIVFAS-UHFFFAOYSA-M tetramethylammonium hydroxide Chemical compound [OH-].C[N+](C)(C)C WGTYBPLFGIVFAS-UHFFFAOYSA-M 0.000 description 10
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 8
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 8
- 239000003518 caustics Substances 0.000 description 8
- 230000000087 stabilizing effect Effects 0.000 description 8
- 239000010936 titanium Substances 0.000 description 8
- 229910052719 titanium Inorganic materials 0.000 description 8
- 229910052725 zinc Inorganic materials 0.000 description 8
- 239000011701 zinc Substances 0.000 description 8
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 7
- 125000002091 cationic group Chemical group 0.000 description 7
- LPSKDVINWQNWFE-UHFFFAOYSA-M tetrapropylazanium;hydroxide Chemical compound [OH-].CCC[N+](CCC)(CCC)CCC LPSKDVINWQNWFE-UHFFFAOYSA-M 0.000 description 6
- 239000004115 Sodium Silicate Substances 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 5
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 5
- 229910052911 sodium silicate Inorganic materials 0.000 description 5
- 229910002493 Ce2(CO3)3 Inorganic materials 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 229910003074 TiCl4 Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000008119 colloidal silica Substances 0.000 description 4
- LVYZJEPLMYTTGH-UHFFFAOYSA-H dialuminum chloride pentahydroxide dihydrate Chemical compound [Cl-].[Al+3].[OH-].[OH-].[Al+3].[OH-].[OH-].[OH-].O.O LVYZJEPLMYTTGH-UHFFFAOYSA-H 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 238000002296 dynamic light scattering Methods 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 238000006116 polymerization reaction Methods 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- VDZOOKBUILJEDG-UHFFFAOYSA-M tetrabutylammonium hydroxide Chemical compound [OH-].CCCC[N+](CCCC)(CCCC)CCCC VDZOOKBUILJEDG-UHFFFAOYSA-M 0.000 description 4
- 229940073455 tetraethylammonium hydroxide Drugs 0.000 description 4
- LRGJRHZIDJQFCL-UHFFFAOYSA-M tetraethylazanium;hydroxide Chemical compound [OH-].CC[N+](CC)(CC)CC LRGJRHZIDJQFCL-UHFFFAOYSA-M 0.000 description 4
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 229910000323 aluminium silicate Inorganic materials 0.000 description 3
- 239000003729 cation exchange resin Substances 0.000 description 3
- 150000001768 cations Chemical class 0.000 description 3
- 229910052681 coesite Inorganic materials 0.000 description 3
- 229910052906 cristobalite Inorganic materials 0.000 description 3
- UAOMVDZJSHZZME-UHFFFAOYSA-N diisopropylamine Chemical compound CC(C)NC(C)C UAOMVDZJSHZZME-UHFFFAOYSA-N 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 229910052682 stishovite Inorganic materials 0.000 description 3
- 229910052905 tridymite Inorganic materials 0.000 description 3
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Inorganic materials [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- 229910016554 Al2(OH)5Cl.2H2O Inorganic materials 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 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
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical group Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 229910052593 corundum Inorganic materials 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010335 hydrothermal treatment Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- 229910052909 inorganic silicate Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 239000011733 molybdenum Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 125000001453 quaternary ammonium group Chemical group 0.000 description 2
- 229910052702 rhenium Inorganic materials 0.000 description 2
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229910052718 tin Inorganic materials 0.000 description 2
- 238000004448 titration Methods 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 2
- 229910001845 yogo sapphire Inorganic materials 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- OQZAQBGJENJMHT-UHFFFAOYSA-N 1,3-dibromo-5-methoxybenzene Chemical compound COC1=CC(Br)=CC(Br)=C1 OQZAQBGJENJMHT-UHFFFAOYSA-N 0.000 description 1
- HSNJERRVXUNQLS-UHFFFAOYSA-N 1-(4-tert-butylphenyl)propan-2-one Chemical compound CC(=O)CC1=CC=C(C(C)(C)C)C=C1 HSNJERRVXUNQLS-UHFFFAOYSA-N 0.000 description 1
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 1
- NJBCRXCAPCODGX-UHFFFAOYSA-N 2-methyl-n-(2-methylpropyl)propan-1-amine Chemical compound CC(C)CNCC(C)C NJBCRXCAPCODGX-UHFFFAOYSA-N 0.000 description 1
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- 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 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 125000005210 alkyl ammonium group Chemical group 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 239000012792 core layer Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000002242 deionisation method Methods 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- JQDCIBMGKCMHQV-UHFFFAOYSA-M diethyl(dimethyl)azanium;hydroxide Chemical compound [OH-].CC[N+](C)(C)CC JQDCIBMGKCMHQV-UHFFFAOYSA-M 0.000 description 1
- 229940043279 diisopropylamine Drugs 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- WEHWNAOGRSTTBQ-UHFFFAOYSA-N dipropylamine Chemical compound CCCNCCC WEHWNAOGRSTTBQ-UHFFFAOYSA-N 0.000 description 1
- JVQOASIPRRGMOS-UHFFFAOYSA-M dodecyl(trimethyl)azanium;hydroxide Chemical compound [OH-].CCCCCCCCCCCC[N+](C)(C)C JVQOASIPRRGMOS-UHFFFAOYSA-M 0.000 description 1
- RDMGYRFGSBZYHW-UHFFFAOYSA-M dodecyl-ethyl-dimethylazanium;hydroxide Chemical compound [OH-].CCCCCCCCCCCC[N+](C)(C)CC RDMGYRFGSBZYHW-UHFFFAOYSA-M 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- WJLUBOLDZCQZEV-UHFFFAOYSA-M hexadecyl(trimethyl)azanium;hydroxide Chemical compound [OH-].CCCCCCCCCCCCCCCC[N+](C)(C)C WJLUBOLDZCQZEV-UHFFFAOYSA-M 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- JJWLVOIRVHMVIS-UHFFFAOYSA-N isopropylamine Chemical compound CC(C)N JJWLVOIRVHMVIS-UHFFFAOYSA-N 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- KTDMLSMSWDJKGA-UHFFFAOYSA-M methyl(tripropyl)azanium;hydroxide Chemical compound [OH-].CCC[N+](C)(CCC)CCC KTDMLSMSWDJKGA-UHFFFAOYSA-M 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 150000002892 organic cations Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 238000013112 stability test Methods 0.000 description 1
- 230000000475 sunscreen effect Effects 0.000 description 1
- 239000000516 sunscreening agent Substances 0.000 description 1
- 125000005207 tetraalkylammonium group Chemical group 0.000 description 1
- DCFYRBLFVWYBIJ-UHFFFAOYSA-M tetraoctylazanium;hydroxide Chemical compound [OH-].CCCCCCCC[N+](CCCCCCCC)(CCCCCCCC)CCCCCCCC DCFYRBLFVWYBIJ-UHFFFAOYSA-M 0.000 description 1
- QVOFCQBZXGLNAA-UHFFFAOYSA-M tributyl(methyl)azanium;hydroxide Chemical compound [OH-].CCCC[N+](C)(CCCC)CCCC QVOFCQBZXGLNAA-UHFFFAOYSA-M 0.000 description 1
- HADKRTWCOYPCPH-UHFFFAOYSA-M trimethylphenylammonium hydroxide Chemical compound [OH-].C[N+](C)(C)C1=CC=CC=C1 HADKRTWCOYPCPH-UHFFFAOYSA-M 0.000 description 1
- YFTHZRPMJXBUME-UHFFFAOYSA-N tripropylamine Chemical compound CCCN(CCC)CCC YFTHZRPMJXBUME-UHFFFAOYSA-N 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/02—Cosmetics or similar toiletry preparations characterised by special physical form
- A61K8/04—Dispersions; Emulsions
- A61K8/042—Gels
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
- A61K8/25—Silicon; Compounds thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/40—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing nitrogen
- A61K8/41—Amines
- A61K8/416—Quaternary ammonium compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
-
- 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
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
-
- 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
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/0004—Preparation of sols
- B01J13/0008—Sols of inorganic materials in water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/141—Preparation of hydrosols or aqueous dispersions
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B37/00—Compounds having molecular sieve properties but not having base-exchange properties
- C01B37/02—Crystalline silica-polymorphs, e.g. silicalites dealuminated aluminosilicate zeolites
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
- A61K2800/10—General cosmetic use
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/64—Nanometer sized, i.e. from 1-100 nanometer
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
Definitions
- the present invention generally relates to colloidal compositions and methods of producing same.
- the present invention relates to colloidal compositions that include a silicate with a metal dispersed within the silicate and at varying metal loadings that can range from as high as about 35 wt % based on silica.
- the colloidal compositions can further include a stabilizer, such as a quaternary compound, that can facilitate the dispersion and loading of the metal within the silicate.
- the present invention provides a novel and unique alternative to conventional surface-treated silica colloids.
- the colloidal compositions of the present invention can be made in any suitable way.
- the colloidal compositions are, in general, synthesized according to two procedures as further detailed below pursuant to various embodiments of the present invention.
- a method of producing a silica colloid includes providing an alkaline solution having a stabilizing component, adding a silicic acid solution to the alkaline solution, and forming a colloid of silica particles wherein the stabilizing component is dispersed throughout each particle. Further, a cationic metal component can be added to the stabilizer-containing alkaline solution in an embodiment. Addition of the silicic acid solution to the alkaline solution thus forms a colloid of silica particles having both the stabilizing component and the metal component dispersed within one or more of the silicate particles, such as in a homogenous manner.
- the stabilizer is a quaternary compound, preferably a quaternary amine, such as a quaternary ammonium hydroxide and the like.
- the stabilizer performs several functions in the synthesis of the colloidal silica.
- the stabilizer provides the OH ⁇ component to the alkaline solution, which catalyzes the reaction between the silicic acid and metal component to form the colloid.
- the stabilizer also enables more of the metal component to bond or chemically combine with the silica component during formation of the colloid.
- the resultant silica colloid demonstrates the capability to carry increased amounts of metal.
- the colloid can have a metal content from about 0.0001 wt % to about 35 wt % based on silica.
- the colloidal particles are amorphous and spherical in shape.
- the colloidal composition can be further processed to produce a crystalline structure as described in greater detail below.
- the diameter of the colloidal particles is in the range of about 2 nm to about 1000 nm according to an embodiment.
- a method of preparing a metal-containing silica colloid wherein a silicic acid solution is reacted with a cationic metal component to form a metal silicate solution.
- the metal silicate solution is subsequently added to an alkaline solution to form a colloid of metal silicate particles.
- Reacting the silicic acid solution with the metal component forms a metal-silicate monomer that is subsequently polymerized as the metal silicate solution is added to the alkaline solution.
- the polymerization forms a homogeneous metal-silicate lattice microstructure or framework throughout the entire solid phase of the colloid.
- the polymerization of the metal-silicate and the utilization of a polyvalent cationic metal component in formation of the colloid yields a metal silicate colloids having metal content in the range of about 0.0001% to as high as 2% by weight silica according to an embodiment.
- the lattice metal-silicate structure throughout the entire solid phase also improves the stability of the colloid.
- the metal silicate colloid of the present invention remains soluble throughout the entire pH range, i.e., pH 1-14.
- the solid phase of the metal silicate colloid of the present invention is substantially amorphous having a generally spherical particle shape and size in the range of from about 2 nm to about 1000 nm according to an embodiment.
- the location of a metal component within the metal-containing silica colloid can be effectively controlled.
- the metal silicate solution and the silicic acid solution can be selectively added to the alkaline solution to form a colloid of silica particles containing metal that is dispersed within one or more of the particles.
- the sequence and duration in which the metal silicate solution and the silicic acid solution are added effectively controls the location of the metal within the solid phase of the colloid.
- the metal silicate solution can be added to the alkaline solution before the silicic acid solution to form a colloid of silica particles having metal dispersed within an interior core layer of each particle.
- the silicic acid solution can be added to the alkaline solution before the metal silicate solution to form a colloid of silica particles having a silica core and metal dispersed within an outer or exterior layer of each particle.
- the metal silicate solution and the silicic acid solution can be added to the alkaline solution in an alternating manner to form a colloid of silica particles having a number of layers, wherein the layers alternate between metal containing layers and layers containing only silica in a repeat or successive manner.
- the present invention provides a colloidal composition.
- the colloidal composition includes a silicate doped with a metal, and a stabilizer dispersed within the silicate.
- the silicate doped with metal includes about 35 wt % or less of metal based on silica.
- the stabilizer includes a quaternary compound.
- the quaternary compound is a quaternary amine.
- an amount of the stabilizer correlates to an amount of the metal.
- the present invention provides a colloidal silicate composition doped with a metal.
- the colloidal silicate composition includes one or more silicate particles wherein the metal is dispersed within one or more of the silicate particles.
- the metal is dispersed in a controlled manner.
- one or more of the silicate particles includes a layered structure.
- the metal is controllably dispersed within one or more particle layers of the layered structure.
- the metal includes an alkali metal, an alkaline earth metal, a 1 st row transition metal, a 2 nd row transition metal, a lanthanide, and combinations thereof.
- the metal is about 2 wt % or less based on silica.
- the present invention provides a method of forming a colloidal composition.
- the method includes preparing a heel solution including a stabilizer; preparing a silicic acid solution; and mixing and further processing the heel solution and the silicic acid solution to form the colloidal composition.
- a metal is added to the heel solution.
- the colloidal composition includes the stabilizer and a silicate doped with the metal such that the stabilizer and the metal are dispersed within one or more particles of the silicate.
- the metal includes about 35 wt % or less based on silica.
- the colloidal composition is further processed to form a crystalline structure.
- the colloidal composition is further processed by heating.
- a metal is added to the heel solution prior to crystallization.
- the colloidal composition includes a zeolite.
- the stabilizer includes a quaternary amine.
- the present invention provides a method of forming a colloidal silicate composition.
- the method includes preparing a silicic acid solution, a metal silicate solution and an alkaline solution; mixing and further processing the silicic acid solution and the metal silicate solution with the alkaline solution; and forming one or more silicate particles doped with a metal wherein the metal is dispersed within one or more of the silicate particles.
- the metal is dispersed in a controlled manner.
- the silica doped with metal includes about 2 wt % or less of the metal based on silica.
- the metal includes an alkali metal, an alkaline earth metal, a 1 st row transition metal, a 2 nd row transition metal, a lanthanide, and combinations thereof.
- a method of controlling a location of a metal within a metal-containing silica colloid includes preparing a silicic acid solution, a metal silicate solution and an alkaline solution; and selectively adding the metal silicate solution and the silicic acid solution to the alkaline solution to form a colloid of silica particles containing the metal.
- the method further comprises adding the metal silicate solution before the silicic acid solution and forming the colloid of silica particles having the metal dispersed within an interior layer of one or more of the silica particles.
- the method further comprises adding the silicic acid solution before the metal silicate solution and forming the colloid of silica particles having the metal dispersed within an outer layer of one or more of the silica particles.
- the method further comprises adding the metal silicate solution and the silicic acid solution in an alternating manner and forming the colloid of silica particles having a metal-containing layer and a non-metal containing layer.
- the silica particles includes a layered structure that has the non-metal containing layer disposed on the metal containing layer in a repeat manner.
- the present invention generally relates to colloidal compositions and methods of preparing same.
- the term “colloid” and other like terms including “colloidal”, “sol”, and the like refer to a two-phase system having a dispersed phase and a continuous phase.
- the colloids of the present invention have a solid phase dispersed or suspended in a continuous or substantially continuous liquid phase, typically an aqueous solution.
- the term “colloid” encompasses both phases whereas “colloidal particles” or “particles” refers to the dispersed or solid phase.
- the present invention relates to colloidal compositions that include a silicate and that can be made in a readily and cost effective manner as described below in greater detail.
- the present invention provides two types of synthesis procedures.
- the present invention utilizes a heel solution that includes a stabilizer, such as a quaternary compound.
- the stabilizer can enhance the colloidal synthesis in a number of ways, such as by stabilizing and better enabling a metal to be dispersed within the silicate of the colloidal composition. It is believed that the stabilizer can also enhance the ability of the silicate to have higher metal loading, such as about 35 wt % or less based on silica.
- silicic acid and a metal silicate solution are selectively added to an alkaline solution thereby producing a colloid that includes a silicate with a metal dispersed therein in a controlled manner.
- a method of preparing a colloidal composition provides adding a silicic acid solution to a reaction vessel that includes a heel solution having an aqueous solution containing a metal component and a stabilizing component to form a colloid of silica particles.
- the stabilizer is an amine or quaternary compound.
- amines suitable for use as the stabilizer include dipropylamine, trimethylamine, triethylmine, tri-n-propylamine, diethanolamine, monoethanolamine, triethanolamine, diisobutylamine, isopropylamine, diisopropylamine, dimethylamine, ethylenediaminetetraacetic acid, pyridine, the like and combinations thereof.
- the stabilizing component is a quaternary amine that forms an alkaline solution when dispersed in water, such as quaternary ammonium hydroxides.
- the quaternary amine includes a tetraalkyl ammonium ion wherein each alkyl group has a carbon chain length of 1 to 10, the alkyl groups being the same or different.
- Nonlimiting examples of quaternary amines suitable for use as the stabilizer include tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH), tetrabutylammonium hydroxide (TBAOH), tetrahexylammonium hydroxide, tetraoctylammonium hydroxide, tributylmethylammonium hydroxide, triethylmethylammonium hydroxide, trimethylphenylammonium hydroxide, methyltripropylammonium hydroxide, dodecyltrimethylammonium hydroxide, hexadecyltrimethylammonium hydroxide, dimethyldodecylethylammonium hydroxide, diethyldimethylammonium hydroxide, the like and combinations thereof.
- TMAOH tetramethylammonium
- the metal can include any suitable material and be derived from any suitable material including metal salts that are soluble or substantially soluble in an aqueous solution.
- the metal includes an alkali metal, an alkaline earth metal, a 1 st row transition metal, a 2 nd row transition metal, a lanthanide, and combinations thereof.
- Preferred metal components include aluminum, cerium, titanium, tin, zirconium, zinc, copper, nickel, molybdenum, iron, rhenium, vanadium, boron, the like and any combination thereof.
- the silicic acid solution can be prepared by passing a sodium silicate solution through a bed of H + -cation exchange resin.
- the resulting deionized silicic acid solution tends to be quite reactive and is typically kept cooled to retard polymerization.
- the disassociated OH ⁇ from the stabilizer catalyzes a polymerization reaction between the cationic metal component and a silicate component from the silicic acid to form the colloid of silica particles.
- the reaction thereby yields a solid phase composed of the metal component, the stabilizer and silica wherein the metal and stabilizer are dispersed within the silica particles.
- Utilization of the stabilizer component obviates the need to provide a heel containing alkaline catalysts, such as NaOH, KOH, NH 4 OH, the like, and combinations thereof. It should be appreciated that any suitable type of silicic acid solution can be utilized.
- the stabilizer serves as a stabilizing agent for the metal component.
- the quaternary amine cation interacts with the metal oxide anion in the heel (MO 4 X ⁇ wherein M is the metal cation) ultimately stabilizing the metal.
- the quaternary amine maintains the metal oxide anion in a four-fold coordination state or tetrahedral orientation so that silicon-to-metal ratios of four can be obtained. Stabilizing the metal component in this manner produces a greater number of silicon-metal linkages allowing the solid phase of the colloid to carry an increased amount of metal compared to surface treated colloids, for example.
- the resultant silica colloid is capable of supporting from about 0.0001 wt % to about 35 wt % metal based on silica.
- the metal-stabilized silica solid phase also demonstrates increased stability and remains stable in a pH range of about 1 to about 14.
- stable means that the solid phase of the colloid is present, dispersed through the medium and stable throughout this entire pH range with effectively no precipitate.
- the solid phase in an embodiment is amorphous and has a number of particles that are generally spherical in shape.
- the colloidal particles have a diameter in the range of about 2 nanometers (nm) to about 1000 nm pursuant to an embodiment.
- silicic acid is utilized to incorporate or disperse a metal component into the framework of colloidal silica (i.e., doping).
- the method includes preparing a heel.
- the heel includes an aqueous solution that at least includes a quaternary amine as defined herein or an alkaline agent. Suitable alkaline agents include, for example, NaOH, KOH, NH 4 OH, the like and combination thereof.
- the silicic acid solution (can be prepared as previously discussed or other suitable manner) is reacted with a cationic metal component to form a metal silicate solution, represented chemically below: H 4 SiO 4 +M x+ ⁇ [x(H 3 SiO 4 ⁇ )-M x+ ]+xH +
- the metal silicate solution is subsequently added to the heel to form the colloid.
- the OH ⁇ present in the heel catalyzes the copolymerization of the cationic metal component and silicate (SiO 4 ⁇ ) from the silicic acid.
- This produces a colloid with the metal dispersed within the silicate i.e., incorporated into the particle framework as discussed above, such as having a homogenous distribution of the metal component throughout the entire solid phase of the colloid.
- the dispersion and loading of the metal is obtained as the copolymerization forms a metal-silicate lattice throughout the microstructure of the solid phase.
- Nonlimiting examples of suitable metals that can be used as the cationic metal component include aluminum, cerium, titanium, tin, zirconium, zinc, copper, nickel, molybdenum, iron, rhenium, vanadium, boron, 1 st and 2 nd row transition metals, lanthanides, alkali metals, alkaline earth metals, the like and any combination thereof.
- the metal component can be derived from any suitable metal source including, for example, any suitable metal salt that is soluble or substantially soluble in an aqueous solution.
- metal silicate colloids of the present invention can have a metal content from about 0.0001% to about 2% by weight based on silica.
- the metal silicate colloids of the present invention are amorphous and generally spherical in shape, wherein the particles have an effective diameter or particle size from about 2 nm to about 1000 nm in an embodiment.
- the metal silicate colloids are stable at a pH range from about 1 to about 14, exhibiting effectively no precipitation in this range.
- the size of the colloidal particles can be adjusted by varying the addition time of the metal silicate solution to the heel.
- the metal silicate solution and the silicic acid solution are selectively added to the heel to control the position of the metal within the solid phase of the colloid as desired.
- Both silicic acid solution and metal silicate solution can be added to the heel to initiate particle formation or to grow or otherwise increase the size of a pure silica particle initially added to the heel.
- the metal silicate solution is added to the heel before the silicic acid solution in an embodiment.
- This addition sequence yields a metal containing silica colloid wherein the metal is dispersed in a core or interior layer of the colloidal particle.
- the subsequent addition of the silicic acid can be used to cover the interior metal-containing portion of the particle with a layer containing on silica without the metal.
- the silicic acid solution can be added to the heel prior to the addition of the metal silicate solution in an embodiment.
- This addition sequence yields colloidal particles having a core or interior composed of silica.
- the metal silicate solution can then be added to coat the silica particle to produce a particle containing metal on an exterior surface or outer layer of the particle wherein the metal is dispersed within this particle layer.
- Addition of only the metal silicate solution to the heel can yield a colloid having a dispersion or distribution of metal within one or more of the colloidal particle as previously discussed.
- Adding the metal silicate solution and the silicic acid solution in an alternating manner or a sequence such as metal silicate-silicic acid-metal silicate-silicic acid can yield a colloidal particle having a number of layers wherein metal containing layers are separated by layers containing silica and without a metal in an embodiment. It will be appreciated that the duration of silicic acid and/or metal silicate addition can be varied as desired to vary the width or thickness of each particle layer in the colloid.
- the multiple layered colloid particles of the present invention are generally spherical in shape and have an effective particle size of about 2 nm to about 1000 nm according to an embodiment.
- colloidal compositions and methods of making same can be modified in any suitable manner.
- the colloidal compositions as described above can be further processed to form a crystalline structure, such as a crystalline silicate, a crystalline metallosilicate including a zeolite, the like and combinations thereof.
- continued hydrothermal treatment at suitable temperatures and over a suitable period of time can produce a more crystalline silicate including metallosilicates, such as zeolites, from the colloidal compositions described-above wherein the colloidal composition includes silicate and a stabilizer with or without a metal dispersed within the silicate, specific examples of which are provided below in greater detail.
- a stabilizer including tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH) and/or the like e.g., a stabilizer including tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH) and/or the like
- TMAOH tetramethylammonium hydroxide
- TPAOH tetrapropylammonium hydroxide
- TEAOH tetraethylammonium hydroxide
- Doped colloidal silica is useful in multitudinous industrial applications including, for example, dental applications, protein separation, molecular sieves, nanoporous membranes, wave guides, photonic crystals, refractory applications, clarification of wine and juice, chemical mechanical planarization of semiconductor and disk drive components, catalyst supports, retention and drainage aids in papermaking, fillers, surface coatings, ceramic materials, investment casting binders, flattening agents, proppants, cosmetic formulations, particularly sunscreens, and polishing abrasives in the glass, optical and electronics and semiconductor industries.
- the form of silica used in a particular application depends in large part on the silica particle's size and porosity characteristics. Doped colloidal silica having the desired characteristics is readily prepared according to the method of this invention.
- this invention is a material for use in an industrial application comprising the colloidal composition described herein.
- the industrial application is selected from the group consisting of catalyst supports, retention and drainage aids in papermaking, fillers, flattening agents, proppants and polishing abrasives.
- a 5 wt % tetramethylammonium hydroxide (20-25 wt %) solution was added to a 12-gallon reactor along with 10.23 wt % of deionized (DI) water.
- DI deionized
- a 0.70 wt % aluminum chlorohydrate (50 wt %) solution was added to 19.82 wt % DI water.
- the aluminum chlorohydrate solution was then added to the reactor at room temperature at a rate of 200 mL/min.
- the reactor was heated to 100° C.
- 64.25 wt % silicic acid was added to the reactor at a ramp rate of 100-220 mL/min over 3.25 hours.
- Table 1 lists the physical characteristics of the colloidal aluminosilicate made in the 12-gallon reactor after it was concentrated by ultra-filtration: TABLE 1 Concentrated Colloidal Aluminosilicate (12 gallon reactor) Results Solids wt % (specific 25.30 gravity) Al 2 O 3 .SiO 2 wt % (ash) 24.72 Solids wt % (removing 29.75 water) “includes organic moiety” PH 11.02 Specific Gravity 1.1671 Conductance (mhos) 7100 Particle Size (nm), 5.00 Titration wt % Al 2 O 3 (BOS), ICP 3.93
- a 0.37 M AlCl 3 .6H 2 O solution was prepared with a pH of 2.2 and was used as prepared as further described below.
- a second solution of 0.50 M AlCl 3 .6H 2 O was prepared. This solution was passed through an ion exchange column containing an anion exchange resin (Dowex 550A (OH ⁇ )). 100 g of AlCl 3 .6H 2 O solution was passed through 100 mL of resin. The pH of the aluminum containing solution was ca. 3.4 after being passed through the column. Aluminum chlorohydrate can also be used.
- the silicic acid solution/monomeric aluminum solution (2.93 g of 0.37 M AlCl 3 .6H 2 O solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.40 g of DI water over a 5.0 hours ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- the silicic acid solution/polyvalent aluminum solution (3.02 g of 0.50 M AlCl 3 .6H 2 O anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.20 g of DI water over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- the silicic acid solution/polyvalent aluminum solution (3.02 g of 0.50 M AlCl 3 .6H 2 O anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.20 g of Example 2 over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- the silicic acid solution/aluminum solution (3.02 g of 0.50 M AlCl 3 .6H 2 O anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.20 g of Example 3 over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- the silicic acid solution/aluminum solution (0.67 g of a 0.87 M solution of aluminum chlorohydrate) was added to a caustic heel containing 0.11 g NaOH (50 wt %) in 3.82 g of 20 nm silica sol in 8.18 g of DI water over a 4.75 hours ramp.
- the reaction was heated at 93° C.
- a total of 87.89 g of silicic acid solution/aluminum solution was added.
- the final product was cation-exchanged to remove excess sodium, large particle filtered (LPC) and pH adjusted to 6.4.
- LPC large particle filtered
- a solution of 0.50 M Ce 2 (CO 3 ) 3 was prepared by adding 46 g Ce 2 (CO 3 ) 3 into 100 ml DI water then adding 1N HCl until dissolved. The solution was then topped up to 200 ml with DI water.
- a silicic acid solution was prepared where 200 g of (sodium silicate) was added to 1000 g of DI water. The solution was passed through a column containing a cation exchange resin (Dowex 650C (H + )). About 40 mL of resin for 100 g of diluted sodium silicate solution was used.
- a cation exchange resin Dowex 650C (H + )
- the silicic acid solution/cerium solution (6.2 ml of 0.5 M Ce 2 (CO 3 ) 3 solution) was added to a caustic heel containing 5 g of KOH (45 wt %) in 200 g of DI water over a 5.0 hours ramp. A total of 1200 g of silicic acid solution/cerium solution was added to produce the cerium doped silica colloids
- a titanium containing solution was prepared.
- a solution of 0.50 M TiCl 4 was prepared by slowly adding 100 ml DI water into a beaker containing 9.4 g TiCl 4 and 10 ml isopropyl alcohol.
- the silicic acid was prepared in the same fashion as described in Example 6. To the silicic acid was added an amount of the titanium containing solution to produce the desired concentration (ppm) of titanium based on silica (BOS) as illustrated below in Table 2.
- the silicic acid solution/titanium solution (12.6 ml of 0.5 M TiCl4 solution) was added to a caustic heel containing 5 g of KOH (45 wt %) in 200 g of DI water over a 5.0 hours ramp. A total of 1200 g of silicic acid solution/cerium solution was added to produce the titanium doped silica colloid.
- the zinc containing solution used in this procedure was a commercially-available product, namely 1N Zn(NO 3 ) 2 .
- the silicic acid was prepared in the same fashion as described in Example 6. To the silicic acid was added an amount of zinc containing solution to provide the desired concentration (ppm) of zinc based on silica (BOS) as illustrated below in Table 2.
- the silicic acid solution/zinc solution (6 ml of 1 M Zn(NO 3 ) 2 solution) was added to a caustic heel containing 5 g of KOH (45 wt %) in 200 g of DI water over a 5.0 hours ramp. A total of 1200 g of acid sol/cerium solution was added to produce the zinc doped silica colloid.
- Colloidal Silicalite-1 was synthesized with a narrow particle size distribution from a mole composition of: 1TPAOH:1.9SiO 2 :109H 2 O
- the source of silica was silicic acid.
- the reactor vessel was charged with a 20-25 wt % solution of TPAOH, which was heated to 90° C. To this, the silicic acid was added over 3 hours. A clear solution resulted, which was heated for 18 hours.
- Colloidal ZSM-5 was synthesized with a narrow particle size distribution from a mole composition of: 65TPAOH:125 SiO 2 :1Al 2 O 3 :7000H 2 O
- the source of silica was silicic acid.
- the reactor vessel was charged with a 20-25 wt % solution of TPAOH, which was heated to 90° C. To this the aluminum/silicic acid solution was added over 2 hours. A clear solution resulted, which was heated for 24 hours.
- Metallosilicate Colloids :
- Table 2 shows the various prepared metal doped samples with the different heels, pH of the different metal containing solutions, amounts of metal added to the acid sol based on silica (BOS) and a variety of characterization techniques to determine particle size and the extent, if any, agglomeration.
- BOS silica
- Table 2 provides a summary of the synthesis procedures according to Examples 1-10 as detailed above: TABLE 2 Theoretical and Particle calculated diameter pH final (ICP) Particle (nm) solution amounts of diameter and (surface [Final wt % Sample Metal source metal QELS and area) m 2 /g metal doped (Heel) and pH BOS a (ppm) (TEM) (nm) Titration Observations SiO 2 ] Example 1 AlCl 3 .6H 2 O 2.2 3,500 (3,281) 47.8 (29.6) 12.9 (233) Prec.
- ICP Theoretical and Particle calculated diameter pH final (ICP) Particle (nm) solution amounts of diameter and (surface [Final wt % Sample Metal source metal QELS and area) m 2 /g metal doped (Heel) and pH BOS a (ppm) (TEM) (nm) Titration Observations SiO 2 ]
- Example 5 Al 2 (OH) 5 Cl.2H 2 O 3,192 (2,446) 49.3 (53.9) 29.4 (102) No prec. 6.87 3.8 [32.7]
- Example 6 Ce 2 (CO 3 ) 3 11650 50.8 No prec. 5.55
- Example 7 TiCl4 3985 45.7 No prec. 5.42
- Example 8 Zn(NO 3 ) 2 5438 No prec. 5.38
- Example 9 — — 241 No prec. 11.5 Silicalite by XRD
- Example 10 Al 2 (OH) 5 Cl.2H 2 O 26000 292 No prec. 11.5 3.8 ZSM-5 byXRD *Aluminum source is anion exchanged to remove chloride and increase pH.
- a BOS means based on silica.
- the metal doped colloids described above and made pursuant to various embodiments exhibit good stability in the pH range 3-9.
- a stability test was conducted on the filtered and cation deionized aluminosilicate colloid of Example 5. The pH was adjusted to 4.1, 6.5 and 8.5 and effective particle diameters were measured (QELS) before and after heat treatment for two weeks at 60° C.
- colloidal compositions of the present invention can be utilized in a number of different and suitable types of applications in any suitable forms and amounts thereof.
- the colloidal composition can be used as a chemical mechanical polishing agent including use for electronic components; a catalyst material and supports thereof including use in the petrochemical industry, such as cracking to increase fractions of gasoline; as a detergent or agent thereof to remove calcium ions and/or the like from solution; and any other types of suitable applications.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Animal Behavior & Ethology (AREA)
- Veterinary Medicine (AREA)
- Public Health (AREA)
- General Health & Medical Sciences (AREA)
- Birds (AREA)
- Epidemiology (AREA)
- Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Nanotechnology (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Crystallography & Structural Chemistry (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- Composite Materials (AREA)
- Dermatology (AREA)
- Silicon Compounds (AREA)
- Colloid Chemistry (AREA)
Abstract
Description
- The present invention generally relates to colloidal compositions and methods of producing same. In particular, the present invention relates to colloidal compositions that include a silicate with a metal dispersed within the silicate and at varying metal loadings that can range from as high as about 35 wt % based on silica. The colloidal compositions can further include a stabilizer, such as a quaternary compound, that can facilitate the dispersion and loading of the metal within the silicate.
- In this regard, the present invention provides a novel and unique alternative to conventional surface-treated silica colloids. The colloidal compositions of the present invention can be made in any suitable way. Preferably, the colloidal compositions are, in general, synthesized according to two procedures as further detailed below pursuant to various embodiments of the present invention.
- According to the first synthesis procedure, a method of producing a silica colloid includes providing an alkaline solution having a stabilizing component, adding a silicic acid solution to the alkaline solution, and forming a colloid of silica particles wherein the stabilizing component is dispersed throughout each particle. Further, a cationic metal component can be added to the stabilizer-containing alkaline solution in an embodiment. Addition of the silicic acid solution to the alkaline solution thus forms a colloid of silica particles having both the stabilizing component and the metal component dispersed within one or more of the silicate particles, such as in a homogenous manner.
- In an embodiment, the stabilizer is a quaternary compound, preferably a quaternary amine, such as a quaternary ammonium hydroxide and the like. The stabilizer performs several functions in the synthesis of the colloidal silica. For example, the stabilizer provides the OH− component to the alkaline solution, which catalyzes the reaction between the silicic acid and metal component to form the colloid. The stabilizer also enables more of the metal component to bond or chemically combine with the silica component during formation of the colloid. The resultant silica colloid demonstrates the capability to carry increased amounts of metal. The colloid can have a metal content from about 0.0001 wt % to about 35 wt % based on silica. The colloidal particles are amorphous and spherical in shape. In addition, the colloidal composition can be further processed to produce a crystalline structure as described in greater detail below. The diameter of the colloidal particles is in the range of about 2 nm to about 1000 nm according to an embodiment.
- According to the second synthesis procedure, a method of preparing a metal-containing silica colloid is provided wherein a silicic acid solution is reacted with a cationic metal component to form a metal silicate solution. The metal silicate solution is subsequently added to an alkaline solution to form a colloid of metal silicate particles. Reacting the silicic acid solution with the metal component forms a metal-silicate monomer that is subsequently polymerized as the metal silicate solution is added to the alkaline solution. The polymerization forms a homogeneous metal-silicate lattice microstructure or framework throughout the entire solid phase of the colloid.
- The polymerization of the metal-silicate and the utilization of a polyvalent cationic metal component in formation of the colloid yields a metal silicate colloids having metal content in the range of about 0.0001% to as high as 2% by weight silica according to an embodiment. The lattice metal-silicate structure throughout the entire solid phase also improves the stability of the colloid. The metal silicate colloid of the present invention remains soluble throughout the entire pH range, i.e., pH 1-14. The solid phase of the metal silicate colloid of the present invention is substantially amorphous having a generally spherical particle shape and size in the range of from about 2 nm to about 1000 nm according to an embodiment.
- With the second synthesis procedure, the location of a metal component within the metal-containing silica colloid can be effectively controlled. The metal silicate solution and the silicic acid solution can be selectively added to the alkaline solution to form a colloid of silica particles containing metal that is dispersed within one or more of the particles. The sequence and duration in which the metal silicate solution and the silicic acid solution are added effectively controls the location of the metal within the solid phase of the colloid. For example, the metal silicate solution can be added to the alkaline solution before the silicic acid solution to form a colloid of silica particles having metal dispersed within an interior core layer of each particle. Alternatively, the silicic acid solution can be added to the alkaline solution before the metal silicate solution to form a colloid of silica particles having a silica core and metal dispersed within an outer or exterior layer of each particle. Moreover, the metal silicate solution and the silicic acid solution can be added to the alkaline solution in an alternating manner to form a colloid of silica particles having a number of layers, wherein the layers alternate between metal containing layers and layers containing only silica in a repeat or successive manner.
- To this end, in an embodiment, the present invention provides a colloidal composition. The colloidal composition includes a silicate doped with a metal, and a stabilizer dispersed within the silicate.
- In an embodiment, the silicate doped with metal includes about 35 wt % or less of metal based on silica.
- In an embodiment, the stabilizer includes a quaternary compound.
- In an embodiment, the quaternary compound is a quaternary amine.
- In an embodiment, an amount of the stabilizer correlates to an amount of the metal.
- In another embodiment, the present invention provides a colloidal silicate composition doped with a metal. The colloidal silicate composition includes one or more silicate particles wherein the metal is dispersed within one or more of the silicate particles.
- In an embodiment, the metal is dispersed in a controlled manner.
- In an embodiment, one or more of the silicate particles includes a layered structure.
- In an embodiment, the metal is controllably dispersed within one or more particle layers of the layered structure.
- In an embodiment, the metal includes an alkali metal, an alkaline earth metal, a 1st row transition metal, a 2nd row transition metal, a lanthanide, and combinations thereof.
- In an embodiment, the metal is about 2 wt % or less based on silica.
- In yet another embodiment, the present invention provides a method of forming a colloidal composition. The method includes preparing a heel solution including a stabilizer; preparing a silicic acid solution; and mixing and further processing the heel solution and the silicic acid solution to form the colloidal composition.
- In an embodiment, a metal is added to the heel solution.
- In an embodiment, the colloidal composition includes the stabilizer and a silicate doped with the metal such that the stabilizer and the metal are dispersed within one or more particles of the silicate.
- In an embodiment, the metal includes about 35 wt % or less based on silica.
- In an embodiment, the colloidal composition is further processed to form a crystalline structure.
- In an embodiment, the colloidal composition is further processed by heating.
- In an embodiment, a metal is added to the heel solution prior to crystallization.
- In an embodiment, the colloidal composition includes a zeolite.
- In an embodiment, the stabilizer includes a quaternary amine.
- In still yet another embodiment, the present invention provides a method of forming a colloidal silicate composition. The method includes preparing a silicic acid solution, a metal silicate solution and an alkaline solution; mixing and further processing the silicic acid solution and the metal silicate solution with the alkaline solution; and forming one or more silicate particles doped with a metal wherein the metal is dispersed within one or more of the silicate particles.
- In an embodiment, the metal is dispersed in a controlled manner.
- In an embodiment, the silica doped with metal includes about 2 wt % or less of the metal based on silica.
- In an embodiment, the metal includes an alkali metal, an alkaline earth metal, a 1st row transition metal, a 2nd row transition metal, a lanthanide, and combinations thereof.
- In a further embodiment, a method of controlling a location of a metal within a metal-containing silica colloid is provided. The method includes preparing a silicic acid solution, a metal silicate solution and an alkaline solution; and selectively adding the metal silicate solution and the silicic acid solution to the alkaline solution to form a colloid of silica particles containing the metal.
- In an embodiment, the method further comprises adding the metal silicate solution before the silicic acid solution and forming the colloid of silica particles having the metal dispersed within an interior layer of one or more of the silica particles.
- In an embodiment, the method further comprises adding the silicic acid solution before the metal silicate solution and forming the colloid of silica particles having the metal dispersed within an outer layer of one or more of the silica particles.
- In an embodiment, the method further comprises adding the metal silicate solution and the silicic acid solution in an alternating manner and forming the colloid of silica particles having a metal-containing layer and a non-metal containing layer.
- In an embodiment, of the silica particles includes a layered structure that has the non-metal containing layer disposed on the metal containing layer in a repeat manner.
- Additional features and advantages of the present invention are described in and will be apparent from the following Detailed Description of the Presently Preferred Embodiments.
- The present invention generally relates to colloidal compositions and methods of preparing same. As used herein, the term “colloid” and other like terms including “colloidal”, “sol”, and the like refer to a two-phase system having a dispersed phase and a continuous phase. The colloids of the present invention have a solid phase dispersed or suspended in a continuous or substantially continuous liquid phase, typically an aqueous solution. Thus, the term “colloid” encompasses both phases whereas “colloidal particles” or “particles” refers to the dispersed or solid phase.
- More specifically, the present invention relates to colloidal compositions that include a silicate and that can be made in a readily and cost effective manner as described below in greater detail. In general, the present invention provides two types of synthesis procedures. In one synthesis procedure, the present invention utilizes a heel solution that includes a stabilizer, such as a quaternary compound. The stabilizer can enhance the colloidal synthesis in a number of ways, such as by stabilizing and better enabling a metal to be dispersed within the silicate of the colloidal composition. It is believed that the stabilizer can also enhance the ability of the silicate to have higher metal loading, such as about 35 wt % or less based on silica. In another synthesis procedure, silicic acid and a metal silicate solution are selectively added to an alkaline solution thereby producing a colloid that includes a silicate with a metal dispersed therein in a controlled manner. The present invention is now described below in greater detail including specific examples that are illustrative of the compositions and methods of the present invention according to various embodiments without limitation.
- In one embodiment of the present invention, a method of preparing a colloidal composition provides adding a silicic acid solution to a reaction vessel that includes a heel solution having an aqueous solution containing a metal component and a stabilizing component to form a colloid of silica particles. In an embodiment, the stabilizer is an amine or quaternary compound. Nonlimiting examples of amines suitable for use as the stabilizer include dipropylamine, trimethylamine, triethylmine, tri-n-propylamine, diethanolamine, monoethanolamine, triethanolamine, diisobutylamine, isopropylamine, diisopropylamine, dimethylamine, ethylenediaminetetraacetic acid, pyridine, the like and combinations thereof. Preferably, the stabilizing component is a quaternary amine that forms an alkaline solution when dispersed in water, such as quaternary ammonium hydroxides. In addition, it is further preferred that the quaternary amine includes a tetraalkyl ammonium ion wherein each alkyl group has a carbon chain length of 1 to 10, the alkyl groups being the same or different. Nonlimiting examples of quaternary amines suitable for use as the stabilizer include tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH), tetrabutylammonium hydroxide (TBAOH), tetrahexylammonium hydroxide, tetraoctylammonium hydroxide, tributylmethylammonium hydroxide, triethylmethylammonium hydroxide, trimethylphenylammonium hydroxide, methyltripropylammonium hydroxide, dodecyltrimethylammonium hydroxide, hexadecyltrimethylammonium hydroxide, dimethyldodecylethylammonium hydroxide, diethyldimethylammonium hydroxide, the like and combinations thereof. Also, the bromide and chloride forms of the above mentioned ammonium salts can be used by passing through a hydroxide (anion)-exchange column to produce the alkylammonium hydroxide materials.
- The metal can include any suitable material and be derived from any suitable material including metal salts that are soluble or substantially soluble in an aqueous solution. In an embodiment, the metal includes an alkali metal, an alkaline earth metal, a 1st row transition metal, a 2nd row transition metal, a lanthanide, and combinations thereof. Preferred metal components include aluminum, cerium, titanium, tin, zirconium, zinc, copper, nickel, molybdenum, iron, rhenium, vanadium, boron, the like and any combination thereof.
- The silicic acid solution can be prepared by passing a sodium silicate solution through a bed of H+-cation exchange resin. The resulting deionized silicic acid solution tends to be quite reactive and is typically kept cooled to retard polymerization. Upon addition of the silicic acid solution to the alkaline solution in the heel, the disassociated OH− from the stabilizer catalyzes a polymerization reaction between the cationic metal component and a silicate component from the silicic acid to form the colloid of silica particles. The reaction thereby yields a solid phase composed of the metal component, the stabilizer and silica wherein the metal and stabilizer are dispersed within the silica particles. Utilization of the stabilizer component obviates the need to provide a heel containing alkaline catalysts, such as NaOH, KOH, NH4OH, the like, and combinations thereof. It should be appreciated that any suitable type of silicic acid solution can be utilized.
- In addition to catalyzing particle formation, the stabilizer serves as a stabilizing agent for the metal component. Not wishing to be bound to any particular theory, it is believed that the quaternary amine cation interacts with the metal oxide anion in the heel (MO4 X− wherein M is the metal cation) ultimately stabilizing the metal. It is believed that the quaternary amine maintains the metal oxide anion in a four-fold coordination state or tetrahedral orientation so that silicon-to-metal ratios of four can be obtained. Stabilizing the metal component in this manner produces a greater number of silicon-metal linkages allowing the solid phase of the colloid to carry an increased amount of metal compared to surface treated colloids, for example.
- In an embodiment, the resultant silica colloid is capable of supporting from about 0.0001 wt % to about 35 wt % metal based on silica. The metal-stabilized silica solid phase also demonstrates increased stability and remains stable in a pH range of about 1 to about 14. The skilled artisan will appreciate that “stable” means that the solid phase of the colloid is present, dispersed through the medium and stable throughout this entire pH range with effectively no precipitate. The solid phase in an embodiment is amorphous and has a number of particles that are generally spherical in shape. The colloidal particles have a diameter in the range of about 2 nanometers (nm) to about 1000 nm pursuant to an embodiment.
- In another embodiment of the present invention, silicic acid is utilized to incorporate or disperse a metal component into the framework of colloidal silica (i.e., doping). The method includes preparing a heel. The heel includes an aqueous solution that at least includes a quaternary amine as defined herein or an alkaline agent. Suitable alkaline agents include, for example, NaOH, KOH, NH4OH, the like and combination thereof. The silicic acid solution (can be prepared as previously discussed or other suitable manner) is reacted with a cationic metal component to form a metal silicate solution, represented chemically below:
H4SiO4+Mx+→[x(H3SiO4 −)-Mx+]+xH+ - The metal silicate solution is subsequently added to the heel to form the colloid. During particle formation, the OH− present in the heel catalyzes the copolymerization of the cationic metal component and silicate (SiO4 −) from the silicic acid. This produces a colloid with the metal dispersed within the silicate (i.e., incorporated into the particle framework as discussed above), such as having a homogenous distribution of the metal component throughout the entire solid phase of the colloid. Not wishing to be bound by any particular theory, it is believed that the dispersion and loading of the metal is obtained as the copolymerization forms a metal-silicate lattice throughout the microstructure of the solid phase. Nonlimiting examples of suitable metals that can be used as the cationic metal component include aluminum, cerium, titanium, tin, zirconium, zinc, copper, nickel, molybdenum, iron, rhenium, vanadium, boron, 1st and 2nd row transition metals, lanthanides, alkali metals, alkaline earth metals, the like and any combination thereof. As previously discussed, the metal component can be derived from any suitable metal source including, for example, any suitable metal salt that is soluble or substantially soluble in an aqueous solution.
- According to this synthesis procedure pursuant to an embodiment, metal silicate colloids of the present invention can have a metal content from about 0.0001% to about 2% by weight based on silica. The metal silicate colloids of the present invention are amorphous and generally spherical in shape, wherein the particles have an effective diameter or particle size from about 2 nm to about 1000 nm in an embodiment. The metal silicate colloids are stable at a pH range from about 1 to about 14, exhibiting effectively no precipitation in this range. The skilled artisan will appreciate that the size of the colloidal particles can be adjusted by varying the addition time of the metal silicate solution to the heel.
- As previously discussed, the above-described synthesis procedure can be utilized to effectively control the location of the method and loading thereof within the colloidal particles. In an embodiment, the metal silicate solution and the silicic acid solution are selectively added to the heel to control the position of the metal within the solid phase of the colloid as desired. Both silicic acid solution and metal silicate solution can be added to the heel to initiate particle formation or to grow or otherwise increase the size of a pure silica particle initially added to the heel. For example, the metal silicate solution is added to the heel before the silicic acid solution in an embodiment. This addition sequence yields a metal containing silica colloid wherein the metal is dispersed in a core or interior layer of the colloidal particle. The subsequent addition of the silicic acid can be used to cover the interior metal-containing portion of the particle with a layer containing on silica without the metal.
- Alternatively, the silicic acid solution can be added to the heel prior to the addition of the metal silicate solution in an embodiment. This addition sequence yields colloidal particles having a core or interior composed of silica. The metal silicate solution can then be added to coat the silica particle to produce a particle containing metal on an exterior surface or outer layer of the particle wherein the metal is dispersed within this particle layer. The skilled artisan will appreciate the myriad of possibilities available for the composition of the colloid solid phase. Addition of only the metal silicate solution to the heel can yield a colloid having a dispersion or distribution of metal within one or more of the colloidal particle as previously discussed. Adding the metal silicate solution and the silicic acid solution in an alternating manner or a sequence such as metal silicate-silicic acid-metal silicate-silicic acid can yield a colloidal particle having a number of layers wherein metal containing layers are separated by layers containing silica and without a metal in an embodiment. It will be appreciated that the duration of silicic acid and/or metal silicate addition can be varied as desired to vary the width or thickness of each particle layer in the colloid. The multiple layered colloid particles of the present invention are generally spherical in shape and have an effective particle size of about 2 nm to about 1000 nm according to an embodiment.
- It should be appreciated that the colloidal compositions and methods of making same can be modified in any suitable manner. For example, the colloidal compositions as described above can be further processed to form a crystalline structure, such as a crystalline silicate, a crystalline metallosilicate including a zeolite, the like and combinations thereof. In an embodiment, continued hydrothermal treatment at suitable temperatures and over a suitable period of time can produce a more crystalline silicate including metallosilicates, such as zeolites, from the colloidal compositions described-above wherein the colloidal composition includes silicate and a stabilizer with or without a metal dispersed within the silicate, specific examples of which are provided below in greater detail.
- According to an embodiment, if the heel in the second synthesis procedure is replaced with an organic cation such as those used in synthesis procedure one (e.g., a stabilizer including tetramethylammonium hydroxide (TMAOH), tetrapropylammonium hydroxide (TPAOH), tetraethylammonium hydroxide (TEAOH) and/or the like), continued hydrothermal treatment after the silicic acid or metal/silicic acid containing solution has been added, can result in the formation of a more crystalline silicate or metallosilicate including a zeolite.
- Doped colloidal silica is useful in multitudinous industrial applications including, for example, dental applications, protein separation, molecular sieves, nanoporous membranes, wave guides, photonic crystals, refractory applications, clarification of wine and juice, chemical mechanical planarization of semiconductor and disk drive components, catalyst supports, retention and drainage aids in papermaking, fillers, surface coatings, ceramic materials, investment casting binders, flattening agents, proppants, cosmetic formulations, particularly sunscreens, and polishing abrasives in the glass, optical and electronics and semiconductor industries. The form of silica used in a particular application depends in large part on the silica particle's size and porosity characteristics. Doped colloidal silica having the desired characteristics is readily prepared according to the method of this invention.
- In an embodiment, this invention is a material for use in an industrial application comprising the colloidal composition described herein.
- In an embodiment, the industrial application is selected from the group consisting of catalyst supports, retention and drainage aids in papermaking, fillers, flattening agents, proppants and polishing abrasives.
- The present invention will be further understood with reference to the following illustrative examples according to various embodiments without limitation.
- Synthesis Procedure One:
- A 5 wt % tetramethylammonium hydroxide (20-25 wt %) solution was added to a 12-gallon reactor along with 10.23 wt % of deionized (DI) water. A 0.70 wt % aluminum chlorohydrate (50 wt %) solution was added to 19.82 wt % DI water. The aluminum chlorohydrate solution was then added to the reactor at room temperature at a rate of 200 mL/min. The reactor was heated to 100° C. Then, 64.25 wt % silicic acid was added to the reactor at a ramp rate of 100-220 mL/min over 3.25 hours. As shown below, Table 1 lists the physical characteristics of the colloidal aluminosilicate made in the 12-gallon reactor after it was concentrated by ultra-filtration:
TABLE 1 Concentrated Colloidal Aluminosilicate (12 gallon reactor) Results Solids wt % (specific 25.30 gravity) Al2O3.SiO2 wt % (ash) 24.72 Solids wt % (removing 29.75 water) “includes organic moiety” PH 11.02 Specific Gravity 1.1671 Conductance (mhos) 7100 Particle Size (nm), 5.00 Titration wt % Al2O3 (BOS), ICP 3.93 - Synthesis Procedure Two:
- 1. Preparation of the Aluminum Containing Solutions
- Monomeric Containing Aluminum Solution:
- A 0.37 M AlCl3.6H2O solution was prepared with a pH of 2.2 and was used as prepared as further described below.
- Polyvalent Aluminum Containing Solution:
- A second solution of 0.50 M AlCl3.6H2O was prepared. This solution was passed through an ion exchange column containing an anion exchange resin (Dowex 550A (OH−)). 100 g of AlCl3.6H2O solution was passed through 100 mL of resin. The pH of the aluminum containing solution was ca. 3.4 after being passed through the column. Aluminum chlorohydrate can also be used.
- 2. Preparation of the Silicic Acid:
- 25.00 g of (sodium silicate) was added to 57.37 g of DI water. The solution was passed through a column containing a cation exchange resin (Dowex 650C (H+)). About 40 mL of resin for 100 g of diluted sodium silicate solution was used to produce a silicic acid solution. To the silicic acid solution, a suitable amount of aluminum containing solution to produce the desired concentration (ppm) of aluminum based on silica (BOS) was added as detailed below in Table 2.
- 3. Preparation of the Metallosilicate Colloids:
- The silicic acid solution/monomeric aluminum solution (2.93 g of 0.37 M AlCl3.6H2O solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.40 g of DI water over a 5.0 hours ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- The silicic acid solution/polyvalent aluminum solution (3.02 g of 0.50 M AlCl3.6H2O anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.20 g of DI water over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- The silicic acid solution/polyvalent aluminum solution (3.02 g of 0.50 M AlCl3.6H2O anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.20 g of Example 2 over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- The silicic acid solution/aluminum solution (3.02 g of 0.50 M AlCl3.6H2O anion-exchanged solution) was added to a caustic heel containing 0.30 g of NaOH (50 wt %) in 14.20 g of Example 3 over a 5.0 hour ramp. A total of 68.57 g of silicic acid solution/aluminum solution was added.
- The silicic acid solution/aluminum solution (0.67 g of a 0.87 M solution of aluminum chlorohydrate) was added to a caustic heel containing 0.11 g NaOH (50 wt %) in 3.82 g of 20 nm silica sol in 8.18 g of DI water over a 4.75 hours ramp. The reaction was heated at 93° C. A total of 87.89 g of silicic acid solution/aluminum solution was added. The final product was cation-exchanged to remove excess sodium, large particle filtered (LPC) and pH adjusted to 6.4.
- A solution of 0.50 M Ce2(CO3)3 was prepared by adding 46 g Ce2(CO3)3 into 100 ml DI water then adding 1N HCl until dissolved. The solution was then topped up to 200 ml with DI water.
- A silicic acid solution was prepared where 200 g of (sodium silicate) was added to 1000 g of DI water. The solution was passed through a column containing a cation exchange resin (Dowex 650C (H+)). About 40 mL of resin for 100 g of diluted sodium silicate solution was used.
- To the silicic acid solution, an amount of the cerium containing solution was added to provide the desired concentration (ppm) of cerium based on silica (BOS) as illustrated in Table 2.
- The silicic acid solution/cerium solution (6.2 ml of 0.5 M Ce2(CO3)3 solution) was added to a caustic heel containing 5 g of KOH (45 wt %) in 200 g of DI water over a 5.0 hours ramp. A total of 1200 g of silicic acid solution/cerium solution was added to produce the cerium doped silica colloids
- A titanium containing solution was prepared. In particular, a solution of 0.50 M TiCl4 was prepared by slowly adding 100 ml DI water into a beaker containing 9.4 g TiCl4 and 10 ml isopropyl alcohol.
- The silicic acid was prepared in the same fashion as described in Example 6. To the silicic acid was added an amount of the titanium containing solution to produce the desired concentration (ppm) of titanium based on silica (BOS) as illustrated below in Table 2.
- The silicic acid solution/titanium solution (12.6 ml of 0.5 M TiCl4 solution) was added to a caustic heel containing 5 g of KOH (45 wt %) in 200 g of DI water over a 5.0 hours ramp. A total of 1200 g of silicic acid solution/cerium solution was added to produce the titanium doped silica colloid.
- The zinc containing solution used in this procedure was a commercially-available product, namely 1N Zn(NO3)2. The silicic acid was prepared in the same fashion as described in Example 6. To the silicic acid was added an amount of zinc containing solution to provide the desired concentration (ppm) of zinc based on silica (BOS) as illustrated below in Table 2. The silicic acid solution/zinc solution (6 ml of 1 M Zn(NO3)2 solution) was added to a caustic heel containing 5 g of KOH (45 wt %) in 200 g of DI water over a 5.0 hours ramp. A total of 1200 g of acid sol/cerium solution was added to produce the zinc doped silica colloid.
- Synthesis Procedure Three. Preparation of crystalline silicate and metallosilicate colloids:
- Colloidal Silicalite-1 was synthesized with a narrow particle size distribution from a mole composition of:
1TPAOH:1.9SiO2:109H2O
The source of silica was silicic acid. The reactor vessel was charged with a 20-25 wt % solution of TPAOH, which was heated to 90° C. To this, the silicic acid was added over 3 hours. A clear solution resulted, which was heated for 18 hours. - Colloidal ZSM-5 was synthesized with a narrow particle size distribution from a mole composition of:
65TPAOH:125 SiO2:1Al2O3:7000H2O
The source of silica was silicic acid. The reactor vessel was charged with a 20-25 wt % solution of TPAOH, which was heated to 90° C. To this the aluminum/silicic acid solution was added over 2 hours. A clear solution resulted, which was heated for 24 hours.
Metallosilicate Colloids: - Table 2 shows the various prepared metal doped samples with the different heels, pH of the different metal containing solutions, amounts of metal added to the acid sol based on silica (BOS) and a variety of characterization techniques to determine particle size and the extent, if any, agglomeration. As shown below, Table 2 provides a summary of the synthesis procedures according to Examples 1-10 as detailed above:
TABLE 2 Theoretical and Particle calculated diameter pH final (ICP) Particle (nm) solution amounts of diameter and (surface [Final wt % Sample Metal source metal QELS and area) m2/g metal doped (Heel) and pH BOSa (ppm) (TEM) (nm) Titration Observations SiO2] Example 1 AlCl3.6H2O 2.2 3,500 (3,281) 47.8 (29.6) 12.9 (233) Prec. 7.68 (H2O/NaOH) [6.54] *Example 2 AlCl3.6H2O 3.4 5,000 (1,508) 28.5 (27.3) 15.3 (196) No prec. 9.60 (H2O/NaOH) anion-exchanged [6.63] *Example 3 AlCl3.6H2O 3.4 5,000 (3,683) 47.9 (51.1) 20.9 (143) No prec. 9.20 anion-exchanged [7.33] *Example 4 AlCl3.6H2O 3.4 5,000 (3,911) 82.8 (89.9) 24.3 (123) No prec. 9.05 anion-exchanged [7.67] Example 5 Al2(OH)5Cl.2H2O 3,192 (2,446) 49.3 (53.9) 29.4 (102) No prec. 6.87 3.8 [32.7] Example 6 Ce2(CO3)3 11650 50.8 No prec. 5.55 Example 7 TiCl4 3985 45.7 No prec. 5.42 Example 8 Zn(NO3)2 5438 No prec. 5.38 Example 9 — — 241 No prec. 11.5 Silicalite by XRD Example 10 Al2(OH)5Cl.2H2O 26000 292 No prec. 11.5 3.8 ZSM-5 byXRD
*Aluminum source is anion exchanged to remove chloride and increase pH.
aBOS means based on silica. Example 5 after cation deionization and pH adjusted to 6.87.
- In general, the metal doped colloids described above and made pursuant to various embodiments exhibit good stability in the pH range 3-9. For example, a stability test was conducted on the filtered and cation deionized aluminosilicate colloid of Example 5. The pH was adjusted to 4.1, 6.5 and 8.5 and effective particle diameters were measured (QELS) before and after heat treatment for two weeks at 60° C. No gelation occurred with these samples after heat treatment and the particle diameters remained essentially the same as demonstrated below in Table 3:
TABLE 3 Particle Diameter Particle Diameter (After Heating @ (Initial) 60° C./two weeks) pH (QELS, nm) (QELS, nm) 4.1 49.6 48.6 6.5 49.6 49.6 8.5 49.6 49.2 - The colloidal compositions of the present invention can be utilized in a number of different and suitable types of applications in any suitable forms and amounts thereof. For example, the colloidal composition can be used as a chemical mechanical polishing agent including use for electronic components; a catalyst material and supports thereof including use in the petrochemical industry, such as cracking to increase fractions of gasoline; as a detergent or agent thereof to remove calcium ions and/or the like from solution; and any other types of suitable applications.
- It should be understood that various changes and modifications to the presently preferred embodiments described herein will be apparent to those skilled in the art. Such changes and modifications can be made without departing from the spirit and scope of the present invention and without diminishing its attendant advantages. It is therefore intended that such changes and modifications be covered by the appended claims.
Claims (31)
Priority Applications (12)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/827,214 US20050234136A1 (en) | 2004-04-19 | 2004-04-19 | Colloidal compositions and methods of preparing same |
KR1020067021598A KR20070027535A (en) | 2004-04-19 | 2005-04-13 | Colloidal composition and preparation method thereof |
PCT/US2005/012371 WO2005104683A2 (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
CA2560748A CA2560748C (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
CN2010102460035A CN101912755B (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
EP05735668.5A EP1744825B1 (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
BRPI0509859-9A BRPI0509859B1 (en) | 2004-04-19 | 2005-04-13 | METHOD FOR CONTROLING A METAL LOCATION WITHIN A SILICA COLLIDE CONTAINING METAL |
JP2007509513A JP5103168B2 (en) | 2004-04-19 | 2005-04-13 | Colloidal composition and method for preparing the same |
SG200902613-9A SG152248A1 (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
CN2005800118801A CN1942237B (en) | 2004-04-19 | 2005-04-13 | Colloidal compositions and methods of preparing same |
TW094112213A TWI377980B (en) | 2004-04-19 | 2005-04-18 | Colloidal compositions and methods of preparing same |
US15/877,168 US10730756B2 (en) | 2004-04-19 | 2018-01-22 | Colloidal compositions and methods of preparing same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/827,214 US20050234136A1 (en) | 2004-04-19 | 2004-04-19 | Colloidal compositions and methods of preparing same |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/877,168 Continuation US10730756B2 (en) | 2004-04-19 | 2018-01-22 | Colloidal compositions and methods of preparing same |
Publications (1)
Publication Number | Publication Date |
---|---|
US20050234136A1 true US20050234136A1 (en) | 2005-10-20 |
Family
ID=35097100
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/827,214 Abandoned US20050234136A1 (en) | 2004-04-19 | 2004-04-19 | Colloidal compositions and methods of preparing same |
US15/877,168 Expired - Lifetime US10730756B2 (en) | 2004-04-19 | 2018-01-22 | Colloidal compositions and methods of preparing same |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/877,168 Expired - Lifetime US10730756B2 (en) | 2004-04-19 | 2018-01-22 | Colloidal compositions and methods of preparing same |
Country Status (10)
Country | Link |
---|---|
US (2) | US20050234136A1 (en) |
EP (1) | EP1744825B1 (en) |
JP (1) | JP5103168B2 (en) |
KR (1) | KR20070027535A (en) |
CN (2) | CN101912755B (en) |
BR (1) | BRPI0509859B1 (en) |
CA (1) | CA2560748C (en) |
SG (1) | SG152248A1 (en) |
TW (1) | TWI377980B (en) |
WO (1) | WO2005104683A2 (en) |
Cited By (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20070034116A1 (en) * | 2005-08-10 | 2007-02-15 | Mac Donald Dennis L | Silica sols with controlled minimum particle size and preparation thereof |
US20070231249A1 (en) * | 2006-04-04 | 2007-10-04 | Francois Batllo | Production and use of polysilicate particulate materials |
US20070282122A1 (en) * | 2006-05-30 | 2007-12-06 | Holland Brian T | Organically modifid silica and use thereof |
WO2007137508A1 (en) * | 2006-05-26 | 2007-12-06 | Anji Microelectronics (Shanghai) Co., Ltd | Polishing slurry for subtle surface planarization and its using method |
US20080085412A1 (en) * | 2006-10-04 | 2008-04-10 | Ortiz C Yolanda | Silica-coated metal oxide sols having variable metal oxide to silica ratio |
US20080108497A1 (en) * | 2006-11-08 | 2008-05-08 | Holland Brian T | Metal-rich siliceous compositions and methods of producing same |
US20080190861A1 (en) * | 2007-02-14 | 2008-08-14 | Branning Merle L | Composition and method for agglomerating solids in solid-liquid separation processes |
US20090018219A1 (en) * | 2005-08-10 | 2009-01-15 | Macdonald Dennis L | Method of producing silica sols with controllable broad size distribution and minimum particle size |
EP2085142A1 (en) * | 2006-11-10 | 2009-08-05 | Yuka Collaboration Corporation | Method for producing coating agent exhibiting photocatalytic activity and coating agent obtained by the same |
US20100146117A1 (en) * | 2008-12-01 | 2010-06-10 | Sebastiaan Hoeksel | Access control for M2M devices in a mobile communication network |
WO2010117949A2 (en) | 2009-04-06 | 2010-10-14 | Nalco Company | Novel approach in controlling dsp scale in the bayer process |
WO2013028958A1 (en) | 2011-08-25 | 2013-02-28 | Basf Corporation | Molecular sieve precursors and synthesis of molecular sieves |
WO2014081607A1 (en) * | 2012-11-25 | 2014-05-30 | Chevron U.S.A. Inc. | Method for preparing cha-type molecular sieves using colloidal aluminosilicate |
US8764974B2 (en) | 2010-04-16 | 2014-07-01 | Nalco Company | Processing aids to improve the bitumen recovery and froth quality in oil sands extraction processes |
WO2014150884A1 (en) * | 2013-03-15 | 2014-09-25 | Ecolab Usa Inc. | Methods of polishing sapphire surfaces |
US9283648B2 (en) | 2012-08-24 | 2016-03-15 | Ecolab Usa Inc. | Methods of polishing sapphire surfaces |
US9302228B2 (en) | 2014-02-28 | 2016-04-05 | Pall Corporation | Charged porous polymeric membrane with high void volume |
US9309126B2 (en) | 2014-02-28 | 2016-04-12 | Pall Corporation | Rapidly dissolvable nanoparticles |
US9446355B2 (en) | 2014-02-28 | 2016-09-20 | Pall Corporation | Porous polymeric membrane with high void volume |
US9561473B2 (en) | 2014-02-28 | 2017-02-07 | Pall Corporation | Charged hollow fiber membrane having hexagonal voids |
US9610548B2 (en) | 2014-02-28 | 2017-04-04 | Pall Corporation | Composite porous polymeric membrane with high void volume |
US9737860B2 (en) | 2014-02-28 | 2017-08-22 | Pall Corporation | Hollow fiber membrane having hexagonal voids |
US9764292B2 (en) | 2014-02-28 | 2017-09-19 | Pall Corporation | Porous polymeric membrane with high void volume |
US9776142B2 (en) | 2014-02-28 | 2017-10-03 | Pall Corporation | Porous polymeric membrane with high void volume |
WO2018111390A1 (en) | 2016-12-13 | 2018-06-21 | Chevron U.S.A. Inc. | Synthesis of molecular sieve ssz-41 |
US10005982B2 (en) | 2015-07-18 | 2018-06-26 | Ecolab Usa Inc. | Chemical additives to improve oil separation in stillage process operations |
US10087081B2 (en) | 2013-03-08 | 2018-10-02 | Ecolab Usa Inc. | Process for producing high solids colloidal silica |
EP3368478A4 (en) * | 2015-10-26 | 2019-06-05 | Ecolab USA Inc. | Highly homogenous zeolite precursors |
US10377014B2 (en) | 2017-02-28 | 2019-08-13 | Ecolab Usa Inc. | Increased wetting of colloidal silica as a polishing slurry |
US10654724B2 (en) | 2016-12-02 | 2020-05-19 | Ecolab Usa Inc. | Polyaluminum salts and their uses in preparation of high-purity colloidal aluminum-silica composite particles and zeolites |
US11384023B2 (en) | 2017-09-26 | 2022-07-12 | Delta Faucet Company | Aqueous gelcasting formulation for ceramic products |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101225282B (en) * | 2007-01-19 | 2013-05-01 | 安集微电子(上海)有限公司 | Low-dielectric material lapping liquid |
GB0922503D0 (en) * | 2009-12-23 | 2010-02-10 | Pilkington Group Ltd | Fire resistant glazings |
CN102344761A (en) * | 2011-08-03 | 2012-02-08 | 南通海迅天恒纳米科技有限公司 | Preparation method of cerium-doped silica sol |
CN105778775B (en) * | 2014-12-23 | 2021-03-02 | 安集微电子(上海)有限公司 | Preparation method of neutral colloidal silicon dioxide |
CN104745146A (en) * | 2015-03-23 | 2015-07-01 | 江苏天恒纳米科技股份有限公司 | Nano-composite abrasive particle sol containing cerium-doped silicon dioxide, polishing agent and preparation method thereof |
CN106867449A (en) * | 2016-12-30 | 2017-06-20 | 上海映智研磨材料有限公司 | A kind of silica Compostie abrasive particles and its production and use |
US12017923B2 (en) * | 2017-07-24 | 2024-06-25 | Prebona Ab | Metal containing formulations |
CN108862215B (en) * | 2018-07-26 | 2020-05-08 | 河钢股份有限公司承德分公司 | Binder for producing vanadium nitride and preparation method thereof |
Citations (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1552341A (en) * | 1921-09-13 | 1925-09-01 | L D Caulk Company | Dental cement and process of making same |
US2736668A (en) * | 1952-05-09 | 1956-02-28 | Du Pont | Process of methoxylating the surface of a siliceous material, and the resulting product |
US2913419A (en) * | 1956-04-18 | 1959-11-17 | Du Pont | Chemical process and composition |
US2974108A (en) * | 1957-01-14 | 1961-03-07 | Du Pont | Aluminosilicate aquasols and their preparation |
US4287086A (en) * | 1975-05-02 | 1981-09-01 | Nl Industries, Inc. | Viscous organic systems containing an organophilic clay gellant without an organic dispersant therefor |
US4410501A (en) * | 1979-12-21 | 1983-10-18 | Snamprogetti S.P.A. | Preparation of porous crystalline synthetic material comprised of silicon and titanium oxides |
US4468023A (en) * | 1981-10-13 | 1984-08-28 | Solloway Daniel S | Aquatic neck exercise assembly |
US4623142A (en) * | 1984-01-31 | 1986-11-18 | Mackechnie Bruce | Hand held, multi-directional device for aquatic exercising |
US4666692A (en) * | 1978-06-22 | 1987-05-19 | Snamprogetti, S.P.A. | Silica-based synthetic material containing titanium in the crystal lattice and process for its preparation |
US4670617A (en) * | 1985-12-30 | 1987-06-02 | Amoco Corporation | Propylation of toluene with a high surface area, zinc-modified, crystalline silica molecular sieve |
US5024826A (en) * | 1990-03-05 | 1991-06-18 | E. I. Du Pont De Nemours And Company | Silica particulate composition |
US5031904A (en) * | 1988-06-20 | 1991-07-16 | Solloway Daniel S | Aquatic boot |
US5221497A (en) * | 1988-03-16 | 1993-06-22 | Nissan Chemical Industries, Ltd. | Elongated-shaped silica sol and method for preparing the same |
US5558851A (en) * | 1992-12-16 | 1996-09-24 | Chevron U.S.A. Inc. | Preparation of aluminosilicate zeolites |
US5597512A (en) * | 1993-10-15 | 1997-01-28 | Nissan Chemical Industries, Ltd. | Method for preparing elongated-shaped silica sol |
US6191323B1 (en) * | 2000-04-25 | 2001-02-20 | Uop Llc | Process for the reduction of ketones and aldehydes to alcohols using a tin substituted zeolite beta |
US6306364B1 (en) * | 1998-12-18 | 2001-10-23 | Uop Llc | Stannosilicate molecular sieves |
US6358882B1 (en) * | 1998-12-08 | 2002-03-19 | The Standard Oil Company | Fluid bed vinyl acetate catalyst |
US6442795B1 (en) * | 2001-01-16 | 2002-09-03 | Girefa Enterprise Co., Ltd. | Damper for a pivot door |
US6669924B1 (en) * | 1999-11-23 | 2003-12-30 | Universite Laval | Mesoporous zeolitic material with microporous crystalline mesopore walls |
US6672993B2 (en) * | 2001-01-12 | 2004-01-06 | Aqualogix, Inc. | Aquatic exercise device |
US20050014000A1 (en) * | 2003-07-18 | 2005-01-20 | Eastman Kodak Company | Cationic shelled particle |
US20070034116A1 (en) * | 2005-08-10 | 2007-02-15 | Mac Donald Dennis L | Silica sols with controlled minimum particle size and preparation thereof |
US20070104643A1 (en) * | 2005-08-05 | 2007-05-10 | Holland Brian T | Mesoporous nanocrystaline zeolite composition and preparation from amorphous colloidal metalosilicates |
US20090018219A1 (en) * | 2005-08-10 | 2009-01-15 | Macdonald Dennis L | Method of producing silica sols with controllable broad size distribution and minimum particle size |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4243828A (en) * | 1963-02-27 | 1981-01-06 | Mobil Oil Corporation | Alkylation of aromatics using a high silica zeolite |
US3442795A (en) * | 1963-02-27 | 1969-05-06 | Mobil Oil Corp | Method for preparing highly siliceous zeolite-type materials and materials resulting therefrom |
EP0109060B1 (en) | 1982-11-10 | 1987-03-11 | MONTEDIPE S.p.A. | Process for the conversion of linear butenes to propylene |
CN1022099C (en) * | 1988-03-16 | 1993-09-15 | 日产化学工业株式会社 | Stable silica sol, and process for preparing it |
JP2803134B2 (en) * | 1988-03-16 | 1998-09-24 | 日産化学工業株式会社 | Elongated silica sol and method for producing the same |
EP0512986A4 (en) * | 1990-01-31 | 1993-04-07 | Industrial Progress, Inc. | Functional complex microgels with rapid formation kinetics |
DE4211050C2 (en) | 1992-04-02 | 1995-10-19 | Siemens Ag | Method of manufacturing a bipolar transistor in a substrate |
US6274112B1 (en) * | 1999-12-08 | 2001-08-14 | E. I. Du Pont De Nemours And Company | Continuous production of silica-based microgels |
JP2003183019A (en) * | 2001-12-18 | 2003-07-03 | Catalysts & Chem Ind Co Ltd | Filtration and separation method of zeolite |
CN1224590C (en) * | 2002-05-22 | 2005-10-26 | 吉林大学 | Preparation method of composite magnetic particle |
-
2004
- 2004-04-19 US US10/827,214 patent/US20050234136A1/en not_active Abandoned
-
2005
- 2005-04-13 JP JP2007509513A patent/JP5103168B2/en active Active
- 2005-04-13 WO PCT/US2005/012371 patent/WO2005104683A2/en active Application Filing
- 2005-04-13 CN CN2010102460035A patent/CN101912755B/en not_active Expired - Fee Related
- 2005-04-13 KR KR1020067021598A patent/KR20070027535A/en active Search and Examination
- 2005-04-13 BR BRPI0509859-9A patent/BRPI0509859B1/en active IP Right Grant
- 2005-04-13 CA CA2560748A patent/CA2560748C/en active Active
- 2005-04-13 CN CN2005800118801A patent/CN1942237B/en active Active
- 2005-04-13 EP EP05735668.5A patent/EP1744825B1/en active Active
- 2005-04-13 SG SG200902613-9A patent/SG152248A1/en unknown
- 2005-04-18 TW TW094112213A patent/TWI377980B/en active
-
2018
- 2018-01-22 US US15/877,168 patent/US10730756B2/en not_active Expired - Lifetime
Patent Citations (27)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1552341A (en) * | 1921-09-13 | 1925-09-01 | L D Caulk Company | Dental cement and process of making same |
US2736668A (en) * | 1952-05-09 | 1956-02-28 | Du Pont | Process of methoxylating the surface of a siliceous material, and the resulting product |
US2913419A (en) * | 1956-04-18 | 1959-11-17 | Du Pont | Chemical process and composition |
US2974108A (en) * | 1957-01-14 | 1961-03-07 | Du Pont | Aluminosilicate aquasols and their preparation |
US4287086A (en) * | 1975-05-02 | 1981-09-01 | Nl Industries, Inc. | Viscous organic systems containing an organophilic clay gellant without an organic dispersant therefor |
US4666692A (en) * | 1978-06-22 | 1987-05-19 | Snamprogetti, S.P.A. | Silica-based synthetic material containing titanium in the crystal lattice and process for its preparation |
US4410501A (en) * | 1979-12-21 | 1983-10-18 | Snamprogetti S.P.A. | Preparation of porous crystalline synthetic material comprised of silicon and titanium oxides |
US4468023A (en) * | 1981-10-13 | 1984-08-28 | Solloway Daniel S | Aquatic neck exercise assembly |
US4623142A (en) * | 1984-01-31 | 1986-11-18 | Mackechnie Bruce | Hand held, multi-directional device for aquatic exercising |
US4670617A (en) * | 1985-12-30 | 1987-06-02 | Amoco Corporation | Propylation of toluene with a high surface area, zinc-modified, crystalline silica molecular sieve |
US5221497A (en) * | 1988-03-16 | 1993-06-22 | Nissan Chemical Industries, Ltd. | Elongated-shaped silica sol and method for preparing the same |
US5031904A (en) * | 1988-06-20 | 1991-07-16 | Solloway Daniel S | Aquatic boot |
US5024826A (en) * | 1990-03-05 | 1991-06-18 | E. I. Du Pont De Nemours And Company | Silica particulate composition |
US5558851A (en) * | 1992-12-16 | 1996-09-24 | Chevron U.S.A. Inc. | Preparation of aluminosilicate zeolites |
US5597512A (en) * | 1993-10-15 | 1997-01-28 | Nissan Chemical Industries, Ltd. | Method for preparing elongated-shaped silica sol |
US6358882B1 (en) * | 1998-12-08 | 2002-03-19 | The Standard Oil Company | Fluid bed vinyl acetate catalyst |
US6306364B1 (en) * | 1998-12-18 | 2001-10-23 | Uop Llc | Stannosilicate molecular sieves |
US6669924B1 (en) * | 1999-11-23 | 2003-12-30 | Universite Laval | Mesoporous zeolitic material with microporous crystalline mesopore walls |
US6191323B1 (en) * | 2000-04-25 | 2001-02-20 | Uop Llc | Process for the reduction of ketones and aldehydes to alcohols using a tin substituted zeolite beta |
US6672993B2 (en) * | 2001-01-12 | 2004-01-06 | Aqualogix, Inc. | Aquatic exercise device |
US20040053749A1 (en) * | 2001-01-12 | 2004-03-18 | Stout Tadlington A. | Aquatic exercise device |
US6442795B1 (en) * | 2001-01-16 | 2002-09-03 | Girefa Enterprise Co., Ltd. | Damper for a pivot door |
US20050014000A1 (en) * | 2003-07-18 | 2005-01-20 | Eastman Kodak Company | Cationic shelled particle |
US20070104643A1 (en) * | 2005-08-05 | 2007-05-10 | Holland Brian T | Mesoporous nanocrystaline zeolite composition and preparation from amorphous colloidal metalosilicates |
US20100104500A1 (en) * | 2005-08-05 | 2010-04-29 | Holland Brian T | Method of manufacturing mesoporous zeolite agglomerates |
US20070034116A1 (en) * | 2005-08-10 | 2007-02-15 | Mac Donald Dennis L | Silica sols with controlled minimum particle size and preparation thereof |
US20090018219A1 (en) * | 2005-08-10 | 2009-01-15 | Macdonald Dennis L | Method of producing silica sols with controllable broad size distribution and minimum particle size |
Non-Patent Citations (2)
Title |
---|
Holland et al, "Dual Templating of Macroporous Silicates with Zeolitic Microporous Frameworks," J. Am. Chem. Soc. 1999, 121, 4308-4309. * |
The Merriam-Webster Unabridged Dictionary., Online @ http://www.merriam-webster.com/dictionary/lattice (copyright 2014), Headword: lattice, layer; p. 1 of 1. * |
Cited By (58)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090018219A1 (en) * | 2005-08-10 | 2009-01-15 | Macdonald Dennis L | Method of producing silica sols with controllable broad size distribution and minimum particle size |
US20070034116A1 (en) * | 2005-08-10 | 2007-02-15 | Mac Donald Dennis L | Silica sols with controlled minimum particle size and preparation thereof |
US8052788B2 (en) | 2005-08-10 | 2011-11-08 | Nalco Company | Method of producing silica sols with controllable broad size distribution and minimum particle size |
US20070231249A1 (en) * | 2006-04-04 | 2007-10-04 | Francois Batllo | Production and use of polysilicate particulate materials |
US10227238B2 (en) * | 2006-04-04 | 2019-03-12 | Ecolab Usa Inc. | Production and use of polysilicate particulate materials |
WO2007137508A1 (en) * | 2006-05-26 | 2007-12-06 | Anji Microelectronics (Shanghai) Co., Ltd | Polishing slurry for subtle surface planarization and its using method |
US20070282122A1 (en) * | 2006-05-30 | 2007-12-06 | Holland Brian T | Organically modifid silica and use thereof |
WO2007143416A3 (en) * | 2006-05-30 | 2008-02-28 | Nalco Co | Organically modified silica and use thereof |
US8372999B2 (en) | 2006-05-30 | 2013-02-12 | Nalco Company | Organically modified silica and use thereof |
CN101454245B (en) * | 2006-05-30 | 2013-01-02 | 纳尔科公司 | Organically modified silica and use thereof |
EP2021282A2 (en) * | 2006-05-30 | 2009-02-11 | Nalco Company | Organically modified silica and use thereof |
US8106229B2 (en) | 2006-05-30 | 2012-01-31 | Nalco Company | Organically modifid silica and use thereof |
EP2021282A4 (en) * | 2006-05-30 | 2012-01-18 | Nalco Co | Organically modified silica and use thereof |
WO2008060768A3 (en) * | 2006-10-04 | 2008-08-07 | Nalco Co | Silica-coated metal oxide sols having variable metal oxide to silica ration |
JP2010505731A (en) * | 2006-10-04 | 2010-02-25 | ナルコ カンパニー | Silica coated metal oxide sol with variable silica to metal oxide ratio |
US20080085412A1 (en) * | 2006-10-04 | 2008-04-10 | Ortiz C Yolanda | Silica-coated metal oxide sols having variable metal oxide to silica ratio |
EP2074061A2 (en) * | 2006-10-04 | 2009-07-01 | Nalco Company | Silica-coated metal oxide sols having variable metal oxide to silica ration |
EP2074061A4 (en) * | 2006-10-04 | 2012-10-10 | Nalco Co | SILICA-COATED METAL OXIDEOLE WITH CHANGING METALXOXIDE / SILICA RATIO |
US20100074974A1 (en) * | 2006-11-08 | 2010-03-25 | Holland Brian T | Metal-rich siliceous compositions and methods of producing same |
US20080108497A1 (en) * | 2006-11-08 | 2008-05-08 | Holland Brian T | Metal-rich siliceous compositions and methods of producing same |
US8003707B2 (en) * | 2006-11-08 | 2011-08-23 | Nalco Company | Metal-rich siliceous compositions and methods of producing same |
EP2079546A2 (en) * | 2006-11-08 | 2009-07-22 | Nalco Company | Metal-rich siliceous compositions and methods of producing same |
EP2079546A4 (en) * | 2006-11-08 | 2012-08-29 | Nalco Co | METALLIC SILICATE COMPOSITIONS AND MANUFACTURING METHOD THEREFOR |
US20100056365A1 (en) * | 2006-11-10 | 2010-03-04 | Yuku Collaboration Corporation | Method for producing coating agent exhibiting photocatalytic activity and coating agent obtained thereby |
EP2085142A4 (en) * | 2006-11-10 | 2011-08-24 | Yuka Collaboration Corp | Method for producing coating agent exhibiting photocatalytic activity and coating agent obtained by the same |
EP2085142A1 (en) * | 2006-11-10 | 2009-08-05 | Yuka Collaboration Corporation | Method for producing coating agent exhibiting photocatalytic activity and coating agent obtained by the same |
US20080190861A1 (en) * | 2007-02-14 | 2008-08-14 | Branning Merle L | Composition and method for agglomerating solids in solid-liquid separation processes |
US20100146117A1 (en) * | 2008-12-01 | 2010-06-10 | Sebastiaan Hoeksel | Access control for M2M devices in a mobile communication network |
WO2010117949A2 (en) | 2009-04-06 | 2010-10-14 | Nalco Company | Novel approach in controlling dsp scale in the bayer process |
US8764974B2 (en) | 2010-04-16 | 2014-07-01 | Nalco Company | Processing aids to improve the bitumen recovery and froth quality in oil sands extraction processes |
WO2013028958A1 (en) | 2011-08-25 | 2013-02-28 | Basf Corporation | Molecular sieve precursors and synthesis of molecular sieves |
US9174849B2 (en) | 2011-08-25 | 2015-11-03 | Basf Corporation | Molecular sieve precursors and synthesis of molecular sieves |
US9283648B2 (en) | 2012-08-24 | 2016-03-15 | Ecolab Usa Inc. | Methods of polishing sapphire surfaces |
US9446493B2 (en) | 2012-08-24 | 2016-09-20 | Ecolab Usa Inc. | Kit for polishing sapphire surfaces |
WO2014081607A1 (en) * | 2012-11-25 | 2014-05-30 | Chevron U.S.A. Inc. | Method for preparing cha-type molecular sieves using colloidal aluminosilicate |
US10087081B2 (en) | 2013-03-08 | 2018-10-02 | Ecolab Usa Inc. | Process for producing high solids colloidal silica |
WO2014150884A1 (en) * | 2013-03-15 | 2014-09-25 | Ecolab Usa Inc. | Methods of polishing sapphire surfaces |
US9896604B2 (en) | 2013-03-15 | 2018-02-20 | Ecolab Usa Inc. | Methods of polishing sapphire surfaces |
EP2969391A4 (en) * | 2013-03-15 | 2017-02-01 | Ecolab USA Inc. | Methods of polishing sapphire surfaces |
US9776142B2 (en) | 2014-02-28 | 2017-10-03 | Pall Corporation | Porous polymeric membrane with high void volume |
US9302228B2 (en) | 2014-02-28 | 2016-04-05 | Pall Corporation | Charged porous polymeric membrane with high void volume |
US9737860B2 (en) | 2014-02-28 | 2017-08-22 | Pall Corporation | Hollow fiber membrane having hexagonal voids |
US9764292B2 (en) | 2014-02-28 | 2017-09-19 | Pall Corporation | Porous polymeric membrane with high void volume |
US9561473B2 (en) | 2014-02-28 | 2017-02-07 | Pall Corporation | Charged hollow fiber membrane having hexagonal voids |
US9446355B2 (en) | 2014-02-28 | 2016-09-20 | Pall Corporation | Porous polymeric membrane with high void volume |
US9610548B2 (en) | 2014-02-28 | 2017-04-04 | Pall Corporation | Composite porous polymeric membrane with high void volume |
US9309126B2 (en) | 2014-02-28 | 2016-04-12 | Pall Corporation | Rapidly dissolvable nanoparticles |
US10005982B2 (en) | 2015-07-18 | 2018-06-26 | Ecolab Usa Inc. | Chemical additives to improve oil separation in stillage process operations |
US10513669B2 (en) | 2015-07-18 | 2019-12-24 | Ecolab Usa Inc. | Chemical additives to improve oil separation in stillage process operations |
EP3368478A4 (en) * | 2015-10-26 | 2019-06-05 | Ecolab USA Inc. | Highly homogenous zeolite precursors |
US10399859B2 (en) | 2015-10-26 | 2019-09-03 | Ecolab Usa Inc. | Highly homogenous zeolite precursors |
US10773967B2 (en) | 2015-10-26 | 2020-09-15 | Ecolab Usa Inc. | Highly homogenous zeolite precursors |
US10934173B2 (en) | 2015-10-26 | 2021-03-02 | Ecolab Usa Inc. | Highly homogenous zeolite precursors |
US10654724B2 (en) | 2016-12-02 | 2020-05-19 | Ecolab Usa Inc. | Polyaluminum salts and their uses in preparation of high-purity colloidal aluminum-silica composite particles and zeolites |
WO2018111390A1 (en) | 2016-12-13 | 2018-06-21 | Chevron U.S.A. Inc. | Synthesis of molecular sieve ssz-41 |
US10377014B2 (en) | 2017-02-28 | 2019-08-13 | Ecolab Usa Inc. | Increased wetting of colloidal silica as a polishing slurry |
US11384023B2 (en) | 2017-09-26 | 2022-07-12 | Delta Faucet Company | Aqueous gelcasting formulation for ceramic products |
US11851376B2 (en) | 2017-09-26 | 2023-12-26 | Delta Faucet Company | Aqueous gelcasting method for ceramic products |
Also Published As
Publication number | Publication date |
---|---|
WO2005104683A3 (en) | 2006-11-30 |
TWI377980B (en) | 2012-12-01 |
CN101912755B (en) | 2012-07-04 |
CN1942237B (en) | 2011-07-06 |
BRPI0509859B1 (en) | 2019-04-24 |
EP1744825B1 (en) | 2019-02-27 |
JP2007532470A (en) | 2007-11-15 |
US20180141822A1 (en) | 2018-05-24 |
CA2560748C (en) | 2013-06-18 |
JP5103168B2 (en) | 2012-12-19 |
EP1744825A2 (en) | 2007-01-24 |
CN101912755A (en) | 2010-12-15 |
EP1744825A4 (en) | 2011-09-07 |
CN1942237A (en) | 2007-04-04 |
SG152248A1 (en) | 2009-05-29 |
WO2005104683A2 (en) | 2005-11-10 |
TW200539935A (en) | 2005-12-16 |
CA2560748A1 (en) | 2005-11-10 |
KR20070027535A (en) | 2007-03-09 |
US10730756B2 (en) | 2020-08-04 |
BRPI0509859A (en) | 2007-10-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10730756B2 (en) | Colloidal compositions and methods of preparing same | |
US8658127B2 (en) | Method of manufacturing mesoporous zeolite agglomerates | |
JP4919948B2 (en) | Synthesis of ZSM-48 crystals by heterostructure non-ZSM-48 seeding | |
US8003707B2 (en) | Metal-rich siliceous compositions and methods of producing same | |
JP5334385B2 (en) | Production and use of polysilicate particulate material | |
US20020090337A1 (en) | Synthesis of zeolites | |
WO2007021402A2 (en) | Silica sols with controlled minimum particle size and preparation thereof | |
CN1092142C (en) | Zeolites and processes for their manufacture | |
JP3577681B2 (en) | Method for producing mesoporous metallosilicate | |
CN117440929B (en) | Method for producing layered silicate and use thereof in production of silica nanosheets | |
JP7530151B2 (en) | Method for producing metal-substituted zeolite | |
JP3828571B2 (en) | Micro particles | |
JP3828571B6 (en) | Micro particles | |
EP0753482A1 (en) | Zeolites and processes for their manufacture | |
WO1997016375A1 (en) | Process for synthesising porous inorganic materials |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: NALCO COMPANY, ILLINOIS Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:HOLLAND, BRIAN T.;BATLLO, FRANCOIS;ORTIZ, CARMEN Y.;AND OTHERS;REEL/FRAME:015674/0956 Effective date: 20040802 |
|
AS | Assignment |
Owner name: BANK OF AMERICA, N.A., AS COLLATERAL AGENT, NEW YO Free format text: SECURITY AGREEMENT;ASSIGNORS:NALCO COMPANY;CALGON LLC;NALCO ONE SOURCE LLC;AND OTHERS;REEL/FRAME:022703/0001 Effective date: 20090513 Owner name: BANK OF AMERICA, N.A., AS COLLATERAL AGENT,NEW YOR Free format text: SECURITY AGREEMENT;ASSIGNORS:NALCO COMPANY;CALGON LLC;NALCO ONE SOURCE LLC;AND OTHERS;REEL/FRAME:022703/0001 Effective date: 20090513 |
|
AS | Assignment |
Owner name: NALCO COMPANY, ILLINOIS Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:BANK OF AMERICA, N.A.;REEL/FRAME:035771/0668 Effective date: 20111201 |
|
AS | Assignment |
Owner name: NALCO COMPANY, ILLINOIS Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:BANK OF AMERICA, N.A.;REEL/FRAME:041808/0713 Effective date: 20111201 |
|
AS | Assignment |
Owner name: ECOLAB USA INC., MINNESOTA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:NALCO COMPANY LLC;CALGON CORPORATION;CALGON LLC;AND OTHERS;REEL/FRAME:041836/0437 Effective date: 20170227 Owner name: NALCO COMPANY LLC, DELAWARE Free format text: CHANGE OF NAME;ASSIGNOR:NALCO COMPANY;REEL/FRAME:041835/0903 Effective date: 20151229 |
|
AS | Assignment |
Owner name: ECOLAB USA INC., MINNESOTA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:NALCO COMPANY;REEL/FRAME:042147/0420 Effective date: 20170227 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |