TW204329B - - Google Patents
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- TW204329B TW204329B TW081104088A TW81104088A TW204329B TW 204329 B TW204329 B TW 204329B TW 081104088 A TW081104088 A TW 081104088A TW 81104088 A TW81104088 A TW 81104088A TW 204329 B TW204329 B TW 204329B
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- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 101
- 239000000463 material Substances 0.000 claims description 75
- 239000000203 mixture Substances 0.000 claims description 51
- 239000011148 porous material Substances 0.000 claims description 44
- 238000001179 sorption measurement Methods 0.000 claims description 35
- 238000000034 method Methods 0.000 claims description 28
- -1 diethylethylphosphine triethoxysilane Chemical compound 0.000 claims description 17
- 125000000217 alkyl group Chemical group 0.000 claims description 12
- 238000001354 calcination Methods 0.000 claims description 11
- 150000001412 amines Chemical class 0.000 claims description 10
- 238000011282 treatment Methods 0.000 claims description 10
- 125000003118 aryl group Chemical group 0.000 claims description 7
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 7
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 5
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 5
- 150000004678 hydrides Chemical class 0.000 claims description 5
- 150000002500 ions Chemical class 0.000 claims description 5
- 150000004820 halides Chemical class 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052796 boron Inorganic materials 0.000 claims description 3
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 claims description 3
- 210000005069 ears Anatomy 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 3
- 229910052719 titanium Inorganic materials 0.000 claims description 3
- 125000003342 alkenyl group Chemical group 0.000 claims description 2
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 230000000737 periodic effect Effects 0.000 claims description 2
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 claims description 2
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 claims 2
- 150000004703 alkoxides Chemical class 0.000 claims 2
- UORVGPXVDQYIDP-UHFFFAOYSA-N borane Chemical compound B UORVGPXVDQYIDP-UHFFFAOYSA-N 0.000 claims 2
- 229910052804 chromium Inorganic materials 0.000 claims 2
- 239000011651 chromium Substances 0.000 claims 2
- PHFQLYPOURZARY-UHFFFAOYSA-N chromium trinitrate Chemical compound [Cr+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PHFQLYPOURZARY-UHFFFAOYSA-N 0.000 claims 2
- PFJFNQUFMTYCHB-UHFFFAOYSA-N C[SiH2]N[SiH3] Chemical compound C[SiH2]N[SiH3] PFJFNQUFMTYCHB-UHFFFAOYSA-N 0.000 claims 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims 1
- 208000001613 Gambling Diseases 0.000 claims 1
- WVEXUUSBAAAPBN-UHFFFAOYSA-N [O-2].C(C)(C)[Al+2] Chemical compound [O-2].C(C)(C)[Al+2] WVEXUUSBAAAPBN-UHFFFAOYSA-N 0.000 claims 1
- 159000000021 acetate salts Chemical class 0.000 claims 1
- YBCVMFKXIKNREZ-UHFFFAOYSA-N acoh acetic acid Chemical compound CC(O)=O.CC(O)=O YBCVMFKXIKNREZ-UHFFFAOYSA-N 0.000 claims 1
- 239000000853 adhesive Substances 0.000 claims 1
- 230000001070 adhesive effect Effects 0.000 claims 1
- JBANFLSTOJPTFW-UHFFFAOYSA-N azane;boron Chemical compound [B].N JBANFLSTOJPTFW-UHFFFAOYSA-N 0.000 claims 1
- 229910000085 borane Inorganic materials 0.000 claims 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims 1
- 239000004327 boric acid Substances 0.000 claims 1
- 229910052791 calcium Inorganic materials 0.000 claims 1
- 239000011575 calcium Substances 0.000 claims 1
- 125000004093 cyano group Chemical group *C#N 0.000 claims 1
- XGZNHFPFJRZBBT-UHFFFAOYSA-N ethanol;titanium Chemical compound [Ti].CCO.CCO.CCO.CCO XGZNHFPFJRZBBT-UHFFFAOYSA-N 0.000 claims 1
- 150000002823 nitrates Chemical class 0.000 claims 1
- 229910000073 phosphorus hydride Inorganic materials 0.000 claims 1
- 230000001568 sexual effect Effects 0.000 claims 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims 1
- 235000013311 vegetables Nutrition 0.000 claims 1
- 235000021419 vinegar Nutrition 0.000 claims 1
- 239000000052 vinegar Substances 0.000 claims 1
- 239000000047 product Substances 0.000 description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 36
- 229910001868 water Inorganic materials 0.000 description 33
- 239000002178 crystalline material Substances 0.000 description 24
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 19
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 17
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 14
- 239000013078 crystal Substances 0.000 description 12
- 239000007789 gas Substances 0.000 description 11
- 229910052757 nitrogen Inorganic materials 0.000 description 11
- FFUAGWLWBBFQJT-UHFFFAOYSA-N hexamethyldisilazane Chemical compound C[Si](C)(C)N[Si](C)(C)C FFUAGWLWBBFQJT-UHFFFAOYSA-N 0.000 description 10
- 239000000126 substance Substances 0.000 description 10
- 238000003756 stirring Methods 0.000 description 9
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 8
- 238000002441 X-ray diffraction Methods 0.000 description 8
- 229910052782 aluminium Inorganic materials 0.000 description 8
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 229910052710 silicon Inorganic materials 0.000 description 8
- 239000010703 silicon Substances 0.000 description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 7
- 150000001875 compounds Chemical class 0.000 description 7
- 238000011049 filling Methods 0.000 description 7
- 238000001914 filtration Methods 0.000 description 7
- 239000002253 acid Substances 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 6
- 239000005416 organic matter Substances 0.000 description 6
- 239000012265 solid product Substances 0.000 description 6
- QEMXHQIAXOOASZ-UHFFFAOYSA-N tetramethylammonium Chemical compound C[N+](C)(C)C QEMXHQIAXOOASZ-UHFFFAOYSA-N 0.000 description 6
- 125000000524 functional group Chemical group 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- AUHZEENZYGFFBQ-UHFFFAOYSA-N 1,3,5-trimethylbenzene Chemical compound CC1=CC(C)=CC(C)=C1 AUHZEENZYGFFBQ-UHFFFAOYSA-N 0.000 description 4
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 239000000356 contaminant Substances 0.000 description 4
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 4
- 238000002309 gasification Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000011777 magnesium Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical class CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000002156 adsorbate Substances 0.000 description 3
- 150000001335 aliphatic alkanes Chemical class 0.000 description 3
- RLGQACBPNDBWTB-UHFFFAOYSA-N cetyltrimethylammonium ion Chemical compound CCCCCCCCCCCCCCCC[N+](C)(C)C RLGQACBPNDBWTB-UHFFFAOYSA-N 0.000 description 3
- 239000004927 clay Substances 0.000 description 3
- 239000010941 cobalt Substances 0.000 description 3
- 229910017052 cobalt Inorganic materials 0.000 description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 3
- 230000002079 cooperative effect Effects 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 150000002367 halogens Chemical class 0.000 description 3
- 229910003480 inorganic solid Inorganic materials 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 229960004029 silicic acid Drugs 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- 125000001424 substituent group Chemical group 0.000 description 3
- 125000000020 sulfo group Chemical group O=S(=O)([*])O[H] 0.000 description 3
- 238000001308 synthesis method Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- FYGHSUNMUKGBRK-UHFFFAOYSA-N 1,2,3-trimethylbenzene Chemical compound CC1=CC=CC(C)=C1C FYGHSUNMUKGBRK-UHFFFAOYSA-N 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical group [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 241000219000 Populus Species 0.000 description 2
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical group O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 238000000921 elemental analysis Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007306 functionalization reaction Methods 0.000 description 2
- 229910052733 gallium Inorganic materials 0.000 description 2
- 229910052736 halogen Inorganic materials 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002808 molecular sieve Substances 0.000 description 2
- 238000006384 oligomerization reaction Methods 0.000 description 2
- 125000000913 palmityl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 229910052698 phosphorus Chemical group 0.000 description 2
- 239000011574 phosphorus Chemical group 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 238000007639 printing Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000011541 reaction mixture Substances 0.000 description 2
- 229910000077 silane Inorganic materials 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910001388 sodium aluminate Inorganic materials 0.000 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 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- RWRDLPDLKQPQOW-UHFFFAOYSA-N tetrahydropyrrole Natural products C1CCNC1 RWRDLPDLKQPQOW-UHFFFAOYSA-N 0.000 description 2
- APSPVJKFJYTCTN-UHFFFAOYSA-N tetramethylazanium;silicate Chemical compound C[N+](C)(C)C.C[N+](C)(C)C.C[N+](C)(C)C.C[N+](C)(C)C.[O-][Si]([O-])([O-])[O-] APSPVJKFJYTCTN-UHFFFAOYSA-N 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- PQDJYEQOELDLCP-UHFFFAOYSA-N trimethylsilane Chemical compound C[SiH](C)C PQDJYEQOELDLCP-UHFFFAOYSA-N 0.000 description 2
- 229910052727 yttrium Inorganic materials 0.000 description 2
- LGXAANYJEHLUEM-UHFFFAOYSA-N 1,2,3-tri(propan-2-yl)benzene Chemical compound CC(C)C1=CC=CC(C(C)C)=C1C(C)C LGXAANYJEHLUEM-UHFFFAOYSA-N 0.000 description 1
- KNKRKFALVUDBJE-UHFFFAOYSA-N 1,2-dichloropropane Chemical compound CC(Cl)CCl KNKRKFALVUDBJE-UHFFFAOYSA-N 0.000 description 1
- DHKVCYCWBUNNQH-UHFFFAOYSA-N 2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]-1-(1,4,5,7-tetrahydropyrazolo[3,4-c]pyridin-6-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NN=C(O1)CC(=O)N1CC2=C(CC1)C=NN2 DHKVCYCWBUNNQH-UHFFFAOYSA-N 0.000 description 1
- YJLUBHOZZTYQIP-UHFFFAOYSA-N 2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C1=NN=C(O1)CC(=O)N1CC2=C(CC1)NN=N2 YJLUBHOZZTYQIP-UHFFFAOYSA-N 0.000 description 1
- 240000002768 Alpinia galanga Species 0.000 description 1
- 240000008564 Boehmeria nivea Species 0.000 description 1
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- POWHBSFCHFEZCH-UHFFFAOYSA-N CCC(C)(CC)O[Si](CC[P+](=O)[O-])(OCC)OCC Chemical compound CCC(C)(CC)O[Si](CC[P+](=O)[O-])(OCC)OCC POWHBSFCHFEZCH-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000270722 Crocodylidae Species 0.000 description 1
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-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
- 240000007839 Kleinhovia hospita Species 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 241000283973 Oryctolagus cuniculus Species 0.000 description 1
- IWYDHOAUDWTVEP-UHFFFAOYSA-N R-2-phenyl-2-hydroxyacetic acid Natural products OC(=O)C(O)C1=CC=CC=C1 IWYDHOAUDWTVEP-UHFFFAOYSA-N 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 244000238515 Thymus pulegioides Species 0.000 description 1
- 235000017715 Thymus pulegioides Nutrition 0.000 description 1
- LEHOTFFKMJEONL-UHFFFAOYSA-N Uric Acid Chemical compound N1C(=O)NC(=O)C2=C1NC(=O)N2 LEHOTFFKMJEONL-UHFFFAOYSA-N 0.000 description 1
- TVWHNULVHGKJHS-UHFFFAOYSA-N Uric acid Natural products N1C(=O)NC(=O)C2NC(=O)NC21 TVWHNULVHGKJHS-UHFFFAOYSA-N 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000001343 alkyl silanes Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- VUEDNLCYHKSELL-UHFFFAOYSA-N arsonium Chemical compound [AsH4+] VUEDNLCYHKSELL-UHFFFAOYSA-N 0.000 description 1
- 229910052789 astatine Inorganic materials 0.000 description 1
- RYXHOMYVWAEKHL-UHFFFAOYSA-N astatine atom Chemical compound [At] RYXHOMYVWAEKHL-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- YOUGRGFIHBUKRS-UHFFFAOYSA-N benzyl(trimethyl)azanium Chemical compound C[N+](C)(C)CC1=CC=CC=C1 YOUGRGFIHBUKRS-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
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Description
經沭部屮央檁準局β工消许合作社印製 -043^9 A 6 _Π_6_ 五、發明説明(3 ) 本發明换鼷於一種藉由将一個或數鹤官能基併入材料 中而改良合成間敝孔材料之方法。 多孔無機固體在工業醮用上,做為催化劑及分離媒有 很大的效益。多孔無機固黼之黴結構之開放可允許分子 接近此等材料之相當大之表面積,因而增進其催化及吸附 活性。以詳細之撇結構為基準來E分,現今使用之多孔材 料可分為三大類。此三大類為非晶形及仲晶形的支撑讎, 結晶性分子籣及改良成靥材料。逋些材料在徽結構上詳細 的差異,明示了其本身在催化吸附行為上及如表面積,細 孔大小及那些大小的變化性,X光嬈射_形的有無,逋些 _的細節及當他們的撇結構藉由透射霣子顯撖鏡及霣子繞 射方法來研究時所得之材料的外觀等用來表現他們的特擻 之各種可見性質的差別之重要差異。 非晶形及仲晶形材料代表多孔無機固臞中重要的一類 ,其在工業應用上,已使用多年。埴些材料的典型例子有 一般使用在催化劑配方之非晶矽石及做為固鼸酸性催化劑 和石油改良催化劑支撑鱺之仲晶遇渡氧化鋁。此處所使用 之“非晶”造艟名讁乃指一種材料其無長距離的次序且可 些徽的誤導,雖然幾乎所有的材料至少在局部範園内都有 某種程度的次序。用來描述逋些材料之另一替代名詞為“ X光無作用的”。矽石的擻結構供由密集的非晶矽石之100 -250A粒子所組成(化學技術Kivk-Othier百科全耆,第三 販,第 20冊,John Vi 丨ey & Sons,紐約,766 - 78 1 頁, 1982),但多孔性像由粒子間的空敝所造成。因為逋些材 (請先間讀背而之注意事項洱填寫本頁) 裝· 訂_ 線· 本紙張尺度逍用中困困家樣準(CNS)肀4規格(210X297公龙) 3 81. 6. 10,000張(Η) 經濟部屮央橾準局貝工消费合作杜印製 Λ 6 _ 4 五、發明説明() 料沒有長距離之次序,細孔大小傾向於分佈在較大範園上 。逋種缺乏次序的情形亦於X光纗射圓形中呈現出來,其 通常是無持色的。 如遇渡氧化鋁之仲晶形材料亦有寬的細孔大小分布, 但較明確之X光繞射麵形通常僳由少許寬峰組成。逋些材 料之微結構你由密緻之氣化鋁相的撖晶匾域所組成且該 材料多孔性你由逭些®域間的不規則孔除所形成的(K Wefers及Chanakya Misra“fg之氣化物及氳氣化物”修 訂技術報告第19號,Alcoa研究實驗室,54 - 59頁,1 987 ) 。因為任一材料中均無長距齷次序去控制其細孔大小,所 以細孔大小之變化性相當离。逋些材料中的细孔大小僳位 在所諝的間鼸孔範圔内,用在本發明上,則為13至2 000 A 之藺。 與逭些結構不明確之固醣成強烈對比的是藉由精確地 重複材料之微細结構的结晶本霣而將其錮孔大小分佈控制 到非常窄之材料。逭些材料稱為”分子篩”,其中最重要 的例子是沸石。大部分彿石的精確晶形撇結構在X光嫌射 匾形中供淸晰的,其_形通常含有許多明確的最大值而得 淸楚無謓地界定此材料。同樣地,由於晶形撇結構的精確 重複性,逭些材料中的細孔大小均非常規則。到目前為止 所發現的所有在嫩鑛孔範圓内(通常聲薷為2至12A)之分 子鐮,其細孔大小鐮報之最大者為約12A。 某些含有其曆两能用膨脹Μ來間隔两的成暦材料,可 予支》以提供具較大程度之多孔性的材料。該成靥材料之 (請先閲讀背而之注意事項#堝寫本頁) 裝. 訂· 線· 本紙張尺度逍用中Β國家橒準(CNS)肀4規格(210X297公;ft) 4 81. 6. Η),000張(Η) 經濟部屮央標準局Μ工消许合作杜印製 L04323 Λ 6 ____Π_6 五、發明説明(5 ) 例子包含黏土。該黏土可用水膨脹,因此黏土層間得以水 分子來間隔開。其他成層材料不能以水來膨脹,但可用某 些如胺類及四级銨化合物等有機膨脹_來膨臛之。此非水 可膨脹之成靥材料的例子换述於美囲專利4,859, 648號中 ,且包含成層砂酸垣,Magadiite, kenyaite,三软酸墙 和鈣鈦確。能用特定之有機膨脹Μ來膨脹的非水可膨脹成 層材料之其他例子則見述於美画専利第4,831,006號中之 含有空位鈦金屬竈材料。 一旦成曆材料膨腥了,該材料可藉由插入如矽石之熱 穩定物質在間隔分離之跚間而予以捸住。前述之美國專利 第4,831,006及4,859, 648號中敘及在此所述之用於支撐 非水可膨脹成靥材料之方法。該經支撑的成靥材料之X光 換射_形態依膨脹或支撑使通常為井然有序的成層撇結構 分裂的程度而有相當大的變化。某些經支撐的成層材料中 之徽結構的規則性會受致《重的破壤,以致在X光繞射圖 形之低角度匾域中僅得看到一個波峰,像在相當於該經支 撑之材料中重複之内層間的d -間隔上。破壤程度較低之材 料在此S域内可顯示出數傭波峰,其通常乃此基本重後之 次序。來自該些靥之晶形結構之X光反射有時亦會看到。 在該些經支撑的成層材料中的細孔大小分佈供比非晶形及 仲晶形材料者窄但比沸石材料的為寬。 在人的世界専利公報第W091/11390號中,已述及一新 潁之無機,多孔,非成層,結晶性材料,得由其大的開孔 之規則性以輿其他纗孔_機固黼有所B別,其細孔大小僳 (請先閲讀背而之注意事項#塡寫本頁) 裝. 訂_ 線- 本紙張尺度逍用中8國家«準(C/»S) Τ4規格(210x297公龙) 5 81. 6. 10,000張(H) 經沭部中央標準局貝工消费合作杜印製 L04323 λ6___Π_66、五、發明説明() 在間敝孔範顯内,因此較類似於非晶形或仲晶形材料的细 大小,但其大小的規則排列及均勻性則較類似於如沸石之 結晶性材料者。尤其是,此新穎種類的材料在煅燒後會里 現在d -間隔大於18埃單位處至少有一鶴波峰和在50t〇rr及 25t:下,苯吸附容量供毎100公克該材料大於15公克苯的 X光繞射_形。 此新種類的分子臃有一_特之性霣,邸在所合成或經 煅燒之材料的细孔颺口内可存在高濃度翹基。本發明的目 的傜在使羥基輿有機處理化合物反鼴以將官能基固定或併 入分子筛材料中。此官能基能在細孔内提供猜待的催化部 位或能作為細孔大小之縮小爾以使細孔大小可依需要來諝 整。 因此,本發明像在於一種改良無機,細孔,非成牖結 晶相材料的方法,此種材料在煅燒後會呈現在d -間隔大於 18埃單位處至少有一個波峰及在6.7Kpa (50 torr)與25t: 下,苯吸附容量為每100公克該材料大於15公克苯的X光繞 射_形,該方法包括在煅燒前後使结晶性材料輿處理組成 物接觸,此組成物你包括M'X’Y'n,其中M’僳選自由元素 週期表之 IIA, IIIA, IVA· VA, VIA, VIIIA, IB, ΙΙΒ, IIIB, IVB, VB及VIB所組成之群者;X’傜龌自曲化物,氫 化物,Ci-6烷氣化物,Ci-ie烷基,Ci -丨8烯基及(:1-18之 芳基,醋酸壤,Cl-18芳基氣化物,磺酸塩及硝酸塲;γ’ 僳選自X’,胺,鱗,硫化物,羰基及氡基;及n = l- 5。 較佳之資例中,此無機,多孔結晶相材料具有直徑至 (請先閱讀背而之注意事項再塡寫本頁) 裝· 線· 本紙*尺度遑用中國國家猱準(CNS)肀4規格(210x297公*) 6 81. 6. 10,000張(H) 經濟部中央標準局Μ工消伢合作社印製 Λ 6 ____Π_6_ 五、發明説明(7 ) 少為約13埃,細孔大小均勻之六角形排列;且在煆燒後, 其六角形«子繞射_形之d1〇〇值大於18埃單位。 有利的是,能直接在經合成的结晶性材料上進行改良 而_須將殘留有檐杨除去。另外,需要的話,能將所有内 部羥基位置官能基化。 本發明之官能基化反應可根鐮下式來描述: Si-O-R^M'X'Y'n............ S ί ΟΙΓ Y,n + R ’ X ’ 其中 S i - 0- R’是结晶性材料晶格内之晶格貼。 R'=H +或R4N + ,其為下述結晶方法中所指之有機嫌離 子。 M'=元素遇期表中 IIA, IIIA. IVA, VA, VIA, VIIIA, IB, IIB, IIIB, IVB, VB或 VIB族之元素( Sargent Welch Scientific Co., Cat, No, S-18806, 1979), M’之較佳元素為 IVA, VIA, VIIIA , IIIB及 IVB族 ,且M'之最佳元素為鈦,絡,雄,鈷,嫌,礪,鋁及矽 〇 X4歯化物,氫化物,磺數1至6之烷氣化物,硪數1 至18之烷基,磺數1至18之芳基•醣酸fi, W數1至18之芳 基氣化物,《(酸塩及碥酸塩。X'之較佳取代基為鹵化物, 磺數1至6之烷氣化物及醏黢竃。 Y·能龌自上述之X’,或胺,除,硫化物,羰基及気基 ,Y’之較佳取代基為該些述於X·者,胺,硫化物及磺數1 至18之烷基,Y’之最佳取代基為該些述於X’者,胺及磺數 1至18之院基;n = l- 5。 (請先閲讀背而之注意事項再填寫本頁) 本紙張尺度逍用中國Β家標準(CNS) Τ4規格(2】0χ297公;¢) 7 81. 6.丨0,000張(H)
043^3 條正 Mm h .二、 Λ6 ㈤九, HG 經濟部中央標準局員工消費合作社印製 五、發明説明($ Μ’Χ’Υ’η之非限定實例包含釀酸络,硝酸络,四乙基 正矽酸垣,四甲基正矽酸壇,四乙氧竑_,異丙氧化鋁,三 -第二丁氧化鋁,六甲基二矽氬烷,二-第二丁氣鋸氣三乙 氧矽烷,二乙基磷乙基三乙氧矽烷,碥酸三甲酯,氯化二 甲基烷基矽烷(基中該烷基含碳數為1至18),氨一砸烷, _烷-四氫呋哺及亞碲酸二甲酷-二溴礪烷。 物質之經處理之組成物對處理組成物之比率,處理期 間及溫度並非重要,其可在大範園内變化。溫度可為-70 υ至250t:, M25C至100 =較佳;時間可從0.1至100小時 ,以0.1至30小時較佳而0.1至24小時為最佳。 該經處理之结晶性材料能就此使用或可進一步加以熱 處理或用如氧氣或一氧化碳之反懕性氣體加以活化。此經 處理之材料可在如NH3, PH3,空氣,〇2, N2, Ar, H2, SiH4或B2H6等反應性或晴性氣體中煅燒。 經處理之结晶性材料可以下式來敘述其具有之官能基 I -S ί 0M Ύ'η I 這些官能化位置可為,例如: 訂- .線丨. 本紙張尺度適用中a园家標準(CNS) f 4規格(210 X 297公釐) 8 (修正頁)81.9.20,000 ,04323 條正’補充. Λ6 ΗΠ -SiOAl 經濟部中央標準局負工消费合作社印¾ 在埴些例子中 Si上之另兩僩鍵沒 能化的晶格黏。 在其煅燒形式 料會示出d-間隔大 X光鏞射匾形(K- 0C 本發明之經煅堍结 係在d-間隔大於的 Cu k- α輻射之2 β 之位置上至少一個 沒有相對強度大.於 ,本發明之煅燒材 下沒有相對強度大 五、發明説明(9 ) 0 -Si0P(0Me)2, -Si0B(0Me)2, -SiOB(Br)2.SMe2, -SiOTi(OEt)3, -SiOCr(acetate)2# -SiOCr(nitrate)2, -SiOSi(OMe)3, -SiOAl(s-OPr)2, -SiOAl(s-OBu)2f -SiOSi(OEt)3,
OEt O
O-S-Bu I -Si〇Si-CH2CH2-P(OEt)2, OSi(OEt)3, OEt -SiOSi(CH3)3, -SiOSi(CH3)2C6H13, -SiOSi(CH3)2C18H37, -SiOSi(CH3)2C6H5. where Me=CH3, Et=C2H5, Pr=C3H7, BU=C4H9. ,-Si代表结晶性材料晶格之晶格酤。 有示出。本發明並非限於該些列出之官 中,利用本發明之方法處理之结晶性材 於約18埃單位之位置上至少一儒波峰之 辐射之2S為4.909度)。更特別的是, 晶之成層材料的特徽可為X光饒射_形 10埃軍位之位置上具有至少兩«波峰( 為.8.842度),在d -間隔大於约18埃單位 波蠔及輿d間隔小於10埃簞位之位置上 最強波峰之約20涔的波峰。更進一步說 料之X光縝射形在d-藺隔10埃單位K 於最強波峰之10涔的波峰。 -------------------J------裝-— ---IT------線 - ~ f=JL?t:il.: i^-a 之:.Η?Ρ^Ι^填·;.·”Ί > 本纸張尺度適用中國园家標準(CNS) 4规格(210 X 297公釐) 9 (修正頁) 81.9.20,000 經濟部屮央標準局β工消#合作社印般 ,043^9 Λ 6 ___RJ_ 五、發明説明1卜) X光繞射數據僳用0-0嫌何學,Cu k-α輻射及能量 分散X光偵測器在Scintag PAD X自動繞射条统上來收集。 使用能量分散X光偵测器得免除對入射或敝光束單光器之 需要。入射及徺射X光光束兩者均僳用雙光_入射及鐃射 準直条统來準直。使用之光櫊大小,從X光管源開始僳分 別為0.5, 1.0, 0.3及0.2··。不同之光檷糸統會産生不同 強度之波峰。具有最大細孔大小之本發明之材料可能需要 較离之準直入射X光光束以便自穿透之入射X光光束分析低 角度波峰。 携射數據像在2Θ為0.04度處逐步掃描來記錄,其中 β為布勒格角度而每步之計算時間為10秒。平面間之間隔 距離,d,僳以埃單位來記算,線的相對強度,1/1〇,(其 中1〇為去背景值後,最強線強度之百分之一)像用曲線擬 合常式導出。該強度並未就洛倫滋(Lorentz)及極化效應 來校正。相對強度表示之符號VS =非常強(75-100), S =強( 50 -7 4 ), b =中度( 2 5 - 49 )及w =弱(0-24)。鏖了解繞射數據 以單線列出也可能隠含多條重叠線在其中,該等重叠線在 特定情況下(如非常高之實驗解析度或結晶改變下)可能會 出現解析線或部分解析線。一般來說,結晶圓的改變能包 含單位晶格參數上之次要改變及/或晶體對稱性上之改變 而其結構並無實質上的變化。逋些次要效醮(包含相對強 度的改變)亦能産生陽離子含董,架構之组成,細孔«充 本質及性霣,熱及/或熱液的經歷·及由於顆粒大小/形狀 效應而産生之波峰宽度/形狀的變化,結構之雜亂或習知X 10 本紙張尺度逍用中國國家榣準(CNS)肀4規格(2丨0X297公龙) 81. 6.】0,000張(H) (請先閲讀背而之注意事項再填寫本頁) 裝. 訂- 線- Λ 6 Π 6 經沭部屮央標準局A工消费合作社印製 五、發明説明V1 ) 光蹺射技蓊者所熟悉的其他因素上的差異。 用本發明之方法處理之材料的另一待揪偽在6.7kpa( 50t〇rr)及25P下,其平衡苯吸附容積為每100公克晶體大 於15公克苯。本材料之平衡苯吸附容積之待性供以沒有細 孔為附隨之污染物阻塞的條件下測量。例如,此吸附試驗 像在具有任何細孔阻塞污染物且水以一般方法移除之結晶 性材料相上實施。水可用如熱處理法之脱水技術移除。細 孔阻绝無檐非晶性材料(如矽石)及有機物可藉與酸或籲或 其他化學試Μ接觸而移除之,因而不利物霣得被移除而對 本發明之晶讎無不利影響。 將本發明之材料在脱水或煅燒,例如450至700 1C ,代 表性的是4501C,至少1鶴小時及其他處理後,如果須要, 可嘗試將細孔阻塞污染物除去,在25t:及50torr下,將苯 與該材料接*直到苯達到平衡以決定平衡苯吸附容量。苯 吸收重量之決定將在下文中更詳細描述之。 利用本發明方法處理之材料通常為間除孔,意指其具 有之均勻細孔愾在13至200埃之大小範鼷内,更常為15至 100埃。在較佳資例中,該材料則具有開放内徑從13至 200埃之大的管道之六方拂列。此結構能藉由透射霣子顯 微鏞及霣子繞射顯示出來。因此,該材料之濂當定向取樣 之《子顯嫩照片示出大管道之六方排列且相對之霣子嫌 射鼸形則顧示出繞射最大值的近似之六方排列。霣子繞射 形之d100間隔是鄰近黏間在六方晶格之hko投彩上之距 離且你闋於透遘di00 = ao 3/2之公式在電子願徽照片上觀 11 本紙*尺度逍用中國B家標準(CNS)甲4規格(210x297公龙) 81. 6. 10,000張(H) (請先間讀背而之注意事項#填寫本頁) 裝- 訂_ Λ 6 η 6 經试部屮央榣準局:〇:工消费合作社印製 五、發明説明1(2 ) 察到之管道間的重複距離ao。在霣子_射_形中看到之 d100間隔相當於在X光繞射_形中低角度波峰(d-間隔大於 18埃)之d-間隔。酋前所得材料之最离等级之製備你在電 子繞射國形中可見到20至40艟不同黏。逭些園形能用100 、110、200、210等之特異之反射之六方hko子集(Subset) 及其相関對稱之反射來標示。 如下所述,通常用於本發明之無檐,非成層間除孔結 晶性材料具有下列組成: Mn/q(Wa Xb Yc Zd Oh) 其中V為如二價之第一列《渡金羼之二價元素,如鏟,鈷 及嫌,及/或鎂,較佳為鈷;X為三價元素,如鋁,硼,雄 及/或鎵,較佳為鋁;Y為四價元素,如矽及/或緒,較佳 為矽;Z為五價元素,如磷;Μ為一或多儀離子,如銨,ΙΑ, ΙΙΑ及VIIB等之離子,通當為氫,納及/或氟離子;η為除 Μ表示氣化物外的組成物之霣荷;<!為》1之加權莫耳平均價 數;n/q為Μ之莫耳數或莫耳分率;a,b,c及d分別為W,X,Y 及Z之莫耳分率;h為1至2.5之數;及(a + b + c + d)=l。 上述之結晶性材料之較佳實例為(a + b + c)大於d,及h = 2時。更佳之實例為a和d = 0,及h = 2時。 在此經合成之形式中,用於本發明之材料*常你在無 水之基礎下,其組成物以下式表示之: rRMn/q(Va Xb Yc Zd Oh) 其中,R為未包含在M離子之SS有櫬材料•及!*為|{之俱數, 邸R之其耳數或莫耳分率。由於Μ及R成分在结晶時的存在 12 本紙張尺度逍用中a Β家榣準(CNS) Τ4規格(210x297公Λ) 81. 6. 10,000張(Η) (請先閱讀背而之注意事項孙塡寫本頁) 裝- 訂- 線<
Λ6 iii; 經濟部t·央標準局員工消費合作社印製 五、發明説明(13 舍使其與該材科 结 合 • 且 易 Μ傅 统之後 结晶 方法 來 移除 戎 取代(在Μ的情況 中 )之。 * 藉本發明之 方 法 處 理 之 超大 细孔结 晶性 材料 之 合成 係 詳述於我們的世 界 專 利 公 報 第W0 9 1 / 1 1 390號中。 尤其是, 具有藉上式來界 定 組 成 之 材 科能 由具有 組成 之氧 化 物之 莫 耳比率係在下列 範 圃 内 之 反 應混 合物來 製備 反應物 可 用 較 佳 WY〇2 0 至 0.5 0.001 至 0.5 x2〇3/(y〇2+z2〇5) 0.1 至 100 0.1 至 20 x2〇3/(Y〇2+w〇+z2〇5) 0.1 至 100 0.1 至 20 Solvent/ (Y〇2+W〇+z2〇5+x2〇3) 1 至 1500 5 至 1000 OH /Y〇2 0 至 10 0 至 5 (M2/e0+R2/f〇)/ (YO +WO+Z 0 5+X2°3) 0·01 至 20 0.05 至 5 M2/e°/ (Y〇2+WO+Z2C 5+X2〇3) 0 至 10 0 至 5 R2/f〇/ (Y〇2+WO+Z2C 5+ΧΛ) 0·01 全 2.0 0.03 至 1-0 其中,e及f分別 為Μ與R之 重 量平 均價數 ,溶 劑為 Ci 至C 6 之 酵類或二酵類, 或 更 佳 為 水 ,及R係包括具有化學式為 RlR2R3R4Q +有櫬 定 向 劑 (其中Q為 氮或磷 )且R 1,R 2 ,R 3及R 4 至少有一者為具 有 碳 數 6至38之芳基或烷基, 如- C6 Η 1 3 , -C 1 α Η 2 1 , - C 1 6 fi 3 3 及 -C 1 8 Η 3 7及其餘各R 1 , R 2 ,R 3 及 R 4係選 自氫及碳數1至5之烷基 〇 該 得自 上述銨 離子 或磷 鐮 子之 化 合物可為氫氧化 物 鹵 化 物 ,矽 酸埴或 其混 合物 〇 與其他已知 之 用 於 直 接 合成 一或多 僩其 他晶 嫌 结構 之 此類試劑相較時 上 述 定 向 _之 特殊功 效. 相信 係 由於 其 裝. 訂· it之;it^-J/llf]-Aa.·'.-', 81.9.20,000 本紙張尺度適用中园國家標準(CNS)甲4峴格(210 X 297公釐) 13 (修正頁) Λ 6 Π 6 經濟部中央標準局A工消f合作杜印製 五、發明説明ί4 ) 在所要之超大細孔材料之成核及成長上有作用如棋板之能 力。道些定向麵之非限制實例包含十六基三甲銨,十六基 三甲«,十八基三甲锇,苯甲基三甲銨•十六基 十四基三甲銨,癸基三甲銨,十二基三甲銨及二甲基雙十 二銨等化合物。 存在該反蠹混合物中之總有機物,R·宜包括上述之 有檐定向爾化學式之銨離子或«離子形式的附加有檐定向 劑,但其中各Ri,R2,R3及IU供遘自氫及含硪數1至5之烷基 (2傾烷基可互相聯結形成琢狀化合物)。該附加之有檐定 向劑之*例包含四甲銨,四乙銨,四丙銨,四丁銨及吡咯 啶竈化合物。第一次提到之有檐定向ίΒ對附加定向劑之比 率範園可從100/1至0.01/1。存有附加有檐定向劑時,在 反醮混合物中之該Κ耳比R2/fO/(Y〇2 + WO + Z2〇S + X2〇3)較佳 為0.1至2.0,最佳為0.12至1.0。 另外,為改變最後结晶相材料之細孔大小,在反鼴混 合物中之總有機物,R,除上述有機定向劑外能包含輔助 有機物。此_助有機物僳灌自(1)芳番族《類及含磺數5至 20之胺類,鹵素及其經d-CM烷基取代之衍生物,(2)單 瓖及多琛脂族經類,含《數5至20之胺類,其經鹵素及d-Cm烷基取代之衍生物及(3)直鍰及支鐽脂族烀類,含磺數 3至16之胺類及其經虐素取代之衍生物。 上述之輔助有機物中,鹵素取代基宜為溴。Cl-Cl4烷 基取代基可為宜鍵或支鍵脂族鍵,如甲基•乙基,丙基, m n m, r m,戊基及其組合。逭些輔助有機物之實例包 (請先閱讀背而之注意事項再填寫本頁) 裝- 訂- 線· 1^紙張尺度遑用中as家樣準(CNS)T4規格(210x297公龙) 14 81. 6. 10,000張(H) Λ 6 Π 6 經床部中央櫺準局ΚΧ工消費合作杜印製 五、發明説明兔5) 含 對二 甲 苯,三甲苯, 乙 苯 及 三 異 丙基 苯 〇 在 反 應混合物中含 有 輔 助 有 機 物時 t 輔 助 有 機 物 / Y0 2之莫耳比為0 . 05至20 , 較佳為0 .1至 1 0 • 而 輔 助 有 機 物 /有機定向翔之莫耳比為0 .02至 100 ,較 佳 為 0 . 05至 35 〇 在 合 成方法中使用 矽 源 時 » 宜 至少 使 用 部 分 有 機 矽 酸 m ,如 四 级銨矽酸壤。 該 矽 m m 之 非限 制 實 例 包 含 四 甲 銨 矽 酸壇 及 四乙基正矽酸 m 〇 上 述 反醮混合物所 用 之 W、 X Y及Z之 各 種 組 之 非 限 制 實例 包 含: V X Y Ζ —- A1 Si - - -- A1 -- Ρ —— A1 Si Ρ Co A1 -- Ρ Co A1 si Ρ -- -- Si - - 包含V之組合為Mg,或選自二價第- -列«渡金屬元素, 如 Hn ,Co 及 Fe; X為 B, Ga 或 Fe 及 Y 為 Ge 〇 為 製 造本發明之結 晶 性 材 料 I 上述 之 反 m 混 合 物 在 所 須 晶體 形 成之期間(通常為5分艟 至 14天 9 較 佳 為 1至300小 畤 ),須保持在25至2 50 1 之 間 » 較 佳為 50至 175¾ , 且Ρ Η 值 宜為9至14。 當 本 發明之結晶性 材 料 為 矽 酸 鋁時 9 合 成 方 法 宜 含 有 下列步* : (請先間讀背而之注意事項再填寫本頁) 裝- 訂- 線- 本紙張尺度边用中a Β家«準(CNS)甲4規格(210x297公龙) 81. 6. 10,000張(H) 15 經沭部中央標準而员工消费合作社印製 Λ 6 ___Ilj6_ 五、發明説明泰6) (1) 將有機(R)定向_輿溶劑或溶麵混合物混合,以使 溶爾/ R2/f0之莫耳比在50至800的範圃内,較佳為50至500 。該混合物構成此合成方法之主要棋板。 (2) 於步* (1)之主要棋板潺合物中加入氣化矽及氣化 鋁,使R2/fO/(Si〇2 + Al2〇3)之比率在0.01至2.0的範園内。 (3) 在20至401C下,攪拌由步*(2)所得之混合物,較 佳為5分鐘至3小時。 (4) 宜在20至50C下,將該混合物靜置予以攪拌或不 »拌10分鏞至24小時。 (5) 在50至150t!下,將從步骤(4>所得之産物結晶, 宜為1至7 2小時。 本發明之處理方法能在催化轉換製程的大範下,用 以增加活性及/或此間除孔結晶性材料之活性及/或S揮性 。逋樣的製程之實例包含裂解及加氫裂解(特別是离分子 量)之离沸或不可蒸籣之進料(尤其是殘餘進料),NOx之邐 原及烯烀之低聚合(例如高黏度潤滑油之製造 >。本發明經 處理遇的材料亦能做為趿附_。 下列的實施例你為更完全地説明本發明之本質及實地 應用。該實施例中,所列之用以輿水,琛已烷,苯及/或 正己烷之吸附容稹做比較之吸附數鐮,他們供為平衡吸附 值,由下列方法得之: 将稱好重量之吸附劑試樣,在約5 40 1C煅燒至少約1小 時及其他處理後(如果霈要,可移除任何細孔阻塞污染物) ,在圾附室中與所需之純吸附爾蒸氣接觸。該吸附劑增加 16 本紙張尺度逍用中a明家樣準(CNS)肀4規格(210X297公;«:) 81. 6. 10,000張(II) (請先閲讀背而之注意事項再構寫本頁) 裝· 、?τ- 線- Λ 6 η 6 經求部屮央榡準局员工消费合作杜印製 五、發明説明(17) 的重量換算為試樣之吸附容積,以克/100克圾附劃來表示 ,其中該吸附劑的重量乃以在約540¾煅煉後者為基準。 本發明之組成物在50Torr(6.7KPa>及25*C下,其平衡苯吸 附容量大於15克/100克,待別是大於17.5克/100,更尤其 是大於約20克/100克。 決定平衡吸附值之較佳方式乃在吸附室中接鼸所需 之純被吸附物蒸氣,該吸附室僳在水蒸氣為1.6kpa(T〇rr) ,正己烷或璨己烷蒸氣為5.31^8(401'〇「「)或苯蒸氣為6.7 kpa(50T〇r*r*),於25TC之情況下,予抽真空至1··以下。在 吸附期間偽藉由氣驩恆定流《裝置控制被吸附物蒸氣的添 加以維持壓力的恆定(在約+0.5β·内)。當結晶性材料吸附 了被吸附物,壓力的降低會使氣體恆定流Λ裝置的閥打開 而讓更多的被吸附物蒸氣進入室中以恢後上述之控制壓力。 當歷力的改變不足以開啓該氣饑恆定流量裝置時,即吸附 已完成。 量测苯吸附數雒之另一方法為適當之熱重分析糸統, 如電臞控制之990/95 1 duPont TGA条统。此吸射繭試樣像 藉在3 5 0 Ί0或5 0 0 1C下加熱來脱水(移除實際吸附的水),以 在流動氩氣中維持重量之恆定。若該試櫬是成經合成之形 式(如含有有機定向劑),則其换於空氣中在約5 4 0它下煅 燒並維持恒定重量,而非前述之35〇υ或500^之處理。在 25t:下,苯吸附之等溫》僳以純氩氣流在適當比例下混合 苯飽和氟氣液來澜量之,以得到所需之苯分壓。苯在6.7 Kpa(50 Torr)之吸附值你由吸附等溫線圏中得之。 17 本紙張尺度遑用中B困家«準(CNS)肀4規格(210X297公釐) 81. 6. 10,000張(H) (請先閱讀背而之注意事項再塡寫本頁) ,〇4紗 五、發明説明(18) 在實施例中•除另有説明外,百分比皆以重量計。 實施例1 將 2.7克之 NaAl〇2(43.5〆 Al2〇3, 30〆 Na2〇)於 146,9 克之水中所成之溶掖輿34.5克NaOH, 189.1克之以29vt〆 氯化Ν,Ν,Ν -三甲基-卜十六烷銨溶液輿遇最之化物樹脂 的氫氛化物,接腾而製得之氫氣化十六基三甲銨游液,以 及110.7克之1111;「83!丨(92涔3丨〇2)混合,攪拌整夜後,將 其置入600CC之离臛蒸汽鍋中,於150TC, 400rp·之攪拌速 度下,反鏖72小時。此混合物具有下列相對莫耳組成: (請先閱讀背而之注意事項再塡寫本頁) 經洧部屮央標準局员工消仰合作杜印製 0 . 25 輿耳 A 1 2 0 3 10 其耳 Na2〇 36 莫耳 S i 〇2 2 . 5 莫耳 (CTMA)2〇 362 .5 莫耳 H2O 遇 濾 此 混合 物 後,由 濾 液中沉澱出之固 黼 産物供以遇 濾 $ 用 水 洗 滌, 然 後在空 氣 中於550它下烺燒10小時來回 收 0 此 經 煅 燒之 産 物證明 有 具有1193«2/g之 表 面稹及下列 以 克 / 1 00克 無水 吸 附兩來 表 示之平衡吸附容 積 : 水 10.2 琢 己 烷 >50 正 己 烷 48.9 苯 68.1 此 試 樣 之煅 燒 産物的 X光繞射形之特撤你包含在 裝· 訂_ 線‘ 本紙張尺度边用中國Η家標準(CNS)甲4規格(210x297公;«:) 81. δ. 10,000張(Η) 18 經濟部屮央櫺準局S:工消伢合作杜印製 Λ6 ___I]JB_ 五、發明説明(19) 50.7±3.0埃之d間隔處有一極強之相對強度線,且在 30.7± 1.0埃處有一弱線。 實施例2 將如實施例1所製備之經煅燒産物0.05克加入經快速 攪拌之有10克氰化三甲基矽烷於15克六甲基二矽氣烷之溶 液中,此混合物於《氣下通流整夜、冷却之、再將試朗以 旋轉蒸發器移除,以兩份10iL之丙酮洗滌該産物後,在空 氣中乾燥邸得到0.53克的産物。 此産物之固態鼸角(i^gic angle)旋轉HMR光譜你用具 質子去偶合之90度鼷衝,在1 200秒間隔下得到,此光譜在 15及-108ρρ·處有波峰。在15ρρ·處之波峰為三甲基單矽院 基[T. Yanagisawa, et al,固體反應性,第五冊,167頁 (1988)]並顯示了産物已反窸。此兩波峰之併合顯示原産 物中有17.9〆的矽已轉化。 三甲基單矽烷化産物之内部細孔龌積你以苯吸附及應 物理吸附兩者來與起始物質之内部細孔黼稹比較。細孔鼸 稹之總減少量以苯测置為48〆而以氫來澜量為34涔。從 CPK分子楔型所澜得TMS基的直徑大約為0.4至0.5πι,因而 在該细孔内面上的TMS基薄而半透明之塗覆應會迪成細孔 直徑減少0.8至1.0η·。該篇等粗線的Horvath-Kowazoe之 變換願示細孔直徑從3.94減少至3.04111(0.90111),符合從 棋型所預澜者。 在氱化三甲基矽烷處理前後得量测水的吸附量,在 3 0 t:下,實施例1之煅燒産物吸附1 0 w t涔的水而該經處理 19 本紙尺度逍用中國Η家標準(CNS)肀4規格(210X297公釐) 81. 6. 10,000張(Η) (請先閲讀背而之注意事項再填寫本頁) 裝. 訂_ 線· c 9 6 6 Λ π 經濟部中央51準局hx工消许合作社印製 五、發明説明(2 的材料則吸附3.3 wt涔的水。此證明了經氱化三甲基矽烷 處理之新颖結基性材料之疏水性會增加。 資施例3 將如實施例1所製備之産物0.5克加入經快速嫌拌之有 15»L六甲基二矽«烷於15克六甲基二矽氣烷之溶掖中,此 混合物在氮氣下邐流整掖,冷却之,再將此試_以旋轉蒸 發器移除,此産物以兩份10iL之丙醑洗滌後,在空氣中乾 嫌即得到0.52克之産物。 用具霣子去禺合之90度脈衝,在1 200秒間隔下,取得 此産物之固態颼角嫵轉Ν Η I{光譜。此光譜在1 5及-1 0 8 p p 處 有波峰,15ρρ·處之波峰為三甲基單矽烷基(Id)並顯示該 産物已反鼴。此二波峰之併合顯示原産物有16.8涔的矽轉 移。在矽- nir*實驗之實驗謓差内,_氯化三甲基矽烷及六 甲基二矽«烷之轉化像同樣的。 實施例2及3顯示用本發明之處理方法之細孔大小的缩 減。 實施例4 將用29wt〆之氨化Ν,Ν,Ν -三甲基-1-十六烷銨溶掖輿 遇量之曲化物樹脂的氫氣化物接》所製得之氫氣化十六基 三甲銨溶液(CTMA)400克與200克之四甲銨(ΤΜΑ)矽酸埴溶 液(矽石=10wt涔· TMA:Si=l:l)合併並攪拌之,然後加入 50克之HiSil,其為含有約6wt〆自由水及約4.5wt〆水合作 用之结合水,且其最终粒徑約為0.02撇米的沉澱水合矽石 ,所得之混合物置於聚丙烯庙中,再放入蒸氣箱(約loot: (請先閲讀背而之注意事項#填寫本頁) 本紙張尺度遑用中a B家樣準(CNS)肀4規格(210X297公釐) 81. 6. 10,000張(H) 20 A 6 η 6 五、發明説明(21) )中48小時。此混合物具有列組成,其像以莫耳/Al2〇3莫 耳來表示: 391 . 4莫耳之S i 〇2 71 . 4莫耳之(CTMA) 2〇 61 . 6其耳之(TMA) 20 9144其耳之H2〇 所得之固體産物傈用遇濾及在室溫下於空氣中乾燥來 回收。此經合成産物之化學分析為: S i 〇2 23.7^ A 1 2 0 3 0.2〆 N 2.3〆 C 33.9^ 灰,lOOOt: 22.1^ (請先閲讀背而之注意事項再塡寫本頁) 裝. 經Μ沟中央標準局Α工消#合作杜印製 實施例5 將實施例4所得之部分産物,繼而在5401C下於氮氣中 煅燒1小時,接蓿於空氣中再煅燒6小時。此材料之苯吸附 JS:為 39.5wt 砵。 實施例6 將由實施例4所得之經空氣乾燥之産物1克輿四乙氣敎 1克在室甅下混合整夜,然後將此混合物輿5克水反應1小 時,此産物在538t:下於氮氣中煅燒1小時,然後在538C 下於空氣中再煅燒6小時。其3〇υ之苯吸附置為25,0以〆 〇 實施例7 線- 本紙張尺度边用中Β國家標準(CNS)T4規格(210X297公;it) 2 1 81. 6. 10,000¾ (H)
經濟部+央51準局A工消t合作社印M 0 4^9 Λ 6 ___Π_6_ 五、發明説明f2) 實施例4之經空氣乾燥産物1克與1克之三-第二丁氣 化鋁在室瀑下混合整夜,再将此混合物輿5克的水反應1小 時,此産物在538*C下於氮氣中煅燒1小時後,再於空氣中 5381C下煅燒6小時,。該30¾之苯吸附量為37.5»t知。 實施例8 將實施例4之經空氣乾燥的産杨10克與二-第二丁氣化 鋁氣基三乙氣矽烷(DBALS)(以1/1之克對克為基準)及50克 之絶對乙醇合併然後混合整夜,此混合物再與100克水合 併並攪拌1小時,然後将所得之固鼸産物用過濾及在空氣 中乾燥來回收,再將此官能基化産物在540 1C下於氮氣中 煅燒1小時,接著再於空氣中煅燒6小時。 實施例9 將實施例4之經空氣乾燥的産物10克與二一第二丁氣 化鋁氣基三乙氣矽烷(DBALS)(以1/1之克對克為基準)及50 克之六甲基二矽氣烷合併然後混合整夜,此混合物再輿 100克水合併再予攪拌1小時,將所得之固讎産物利用遇濾 及在室溫下於空氣中乾燥來囲收。接箸将此官能基化産物 在540它下於氮氣中煅嫌1小時後,再於空氣中煅燒6小時 〇 實施例10 將實施例4之經空氣乾燥的産物10克與二乙基乙麟三 乙氣矽烷(以1/1之克對克為基準)及50克之绝對乙酵合併 然後予以混合整夜,再將此混合物與100克水合併後,予 攪拌1小時,将所得之固體産物利用«濾及在室溫下於空 (請先閲讀背而之注意事項再塡寫本頁) 裝- 線. 本紙張尺度边用中國困家標準(CNS)肀4規格(210x297公龙) 22 81. 6. 10,000張(H) 經沭部中央標準局β工消费合作社印製 五、發明説明f 3 ) 氣中乾燥來回收,繼而將此官能基化産物在5 4〇υ下於氮 氣中煅燒1小時,接著再於空氣中煅燒6小時。 實施例11 將實施例4之經空氣乾嫌的産物10克輿碾酸三甲酯(以 2/1之克對克為基準及50克之绝對乙酵合併,然後予以混 合整夜,將此混合物輿100克水合併後,再予攪拌1小時, 所得之固體産物利用邊濾及在室溫下於空氣中乾嫌而固收 後,將此官能基化産物在540 1C下於氡氣中煅燒1小時,接 蓿再於空氣中煅嫌6小時。 實施例12 將實施例4之經空氣乾燥的産物10克舆異丙氣化鋁 7.5克及50克绝對乙酵合併,然後予以混合整夜,接而將 此混合物100克水合併再予攪拌1小時,所得之固體産物利 用過濾及在室灑下於空氣中乾嫌回收後,再將此官能基化 産物在54〇υ下於《氣中煅燒1小時,接著於空氣中再煅燒 6小時。 比較實施例4之未經處理的産物輿資施例8-12之經處 理的産物之元素分析,結果列於表1中。 (請先閲讀背而之注意寧項洱蜞寫本頁) 本紙張尺度逍用中a國家楳準(CNS)甲4規格(210x297公;it) 23 81. 6.丨0,000張(Η) 五、發明説明(2 4) Λ 6 Β 6 表 合 成 産 物 之 元 素分 析 C Ν Si A 1 P B 灰 (1 000 實 施 例 4 33 . 0 2 .32 10 . 9 0.052 - - 22 .1 實 施 例 8 - - 25 . 9 11.2 - - 77 .0 實 施 例 9 - - 32 . 3 5.2 - - 84 .5 實 施 例 10 - - 32 . 9 - 4 . 7 - 74 .3 實 施 例 11 - - 32 . 1 - - 2 · 6 76 .3 實 施 例 12 - - 16. 2 17.7 - 80 .8 實 施 例 6- 12說 明 其 他型 式 之能用本 發明 之方法 將 之 併 入 該 結 晶 性 材 料 中 的 官 能基 〇
先 背 而 之 注 意 事 項 再 堝 % 本 I 裝 經濟部屮央標準局s:工消#合作社印製 實施例13 在此實施例中.愾將NaAl〇2 1.65克加入80克之氫氣 化十六基三甲銨(CTMA0H)溶液中(該溶液像以29vt〆之氰 化Ν,Ν,Ν -三甲基-1-十六烷銨溶液與鹵化物交換樹脂之氫 氣化物接«所製得)攪拌此潺合物直到Na/U〇2完全溶解為 止,再於此溶液中加入40克之四甲銨矽酸塩溶液(10wt涔 81〇2),10克之111511(9〇¥1:涔51〇2)及6.01克之1,3,5-三甲 苯,所得之混合物於室粗下攪拌數分鐘,然後將此凝謬置 入300bL之高壓蒸氣鍋中,接著加熱至105C,同時以 150RPM之轉速攪拌之,在加熱約4小時後,以冷水驟冷此 反醮,再將産物取出,將此産物遇濾並以瀑熱蒸籣水(60-7〇υ)及丙酮洗滌數次後,將最終産物在538υ下於N2空氣 混合氣羅中煅燒8小時。此»謬反醮混合物具有下列之組 η 線 卜紙张尺度逍用中國Η家榣準(CNS)甲4規格(210x297公龙) 24 81. 6. 10,000張(Η) 經濟部中央摇準局C3:工消"合作社印製 L㈣沾 Λ 6 ___Π_6_ 五、發明説明¢5) 成•其你以其耳/ AI2O3莫耳來表示: 1.25 莫耳 Na2〇 27.8 莫耳 Si〇2 5.1 莫耳 (CTMA)2〇 2.24 莫耳 (TMA>20 650 莫耳 H2〇 6.91 莫耳 1,3,5-三甲苯 此實施例之煅燒産物證明其有948.6l|2/g之表面積及 64.0vt>之苯吸附容積。 實施例14 將實施例13之産物1克與正矽酸四乙酯在室租下混合 整夜,然後將此混合物與5克水反*1小時,所得到之産物 在5381C下於氮氣中予以煅燒1小時,再於空氣中,538C 下煅燒6小時,251C之苯吸附量為40.0wt乂。因為此結晶 性材料具有之初始苯吸附量為64,Owt涔,細孔酸稹遂減少 37〆,即細孔直徑減少了 8埃。 實施例15 於溶於30克蒸鱷水之18.7克矽酸納(Ha -砂酸雇)中加 入溶於10克水之1.2克硫酸,將所得之混合物攪拌分嫌 後,加入溶於50.2克水中之16,77克溴化十六基三甲敍,接 著將所得之凝腰攪拌0.5小時,此時,加入20克的水於該 反窿中,然後讓此凝謬於聚丙烯瓶中(100¾)在靜態,自 生的情況下結晶;所得産物以蒸籣水擻底地洗滌,乾燥之 ,再於538t:下煅燒。本實施例之經煅燒的産物之X光燒条 (請先閱讀背而之注意事項再塥寫本頁) 裝. ,?τ_ 線- 本紙張尺度逍用中a國家標準(CNS) T4規格(210x297公*) 25 81. 6. 10,000張(H) Λ 6 Π 6 經濟部中央標準局员工消费合作社印^ 五、發明説明 <26) 形包含在d間颺為33.2±2.0埃處有一甚毪之相對強度線 及在19.8± 1.0埃輿17.5± 1.0埃處有弱線。此材料之苯吸 附ϋ為50涔。 資施例16 將實施例15之産物0.5克與在20iL之甲苯中的(CHa)2 S:BH3 IOiL合併,攪拌約5分鐘後,真空遍濾分離出固體, 接而以正己烷洗籌,再以丙_洗滌,然後將此乾燥産物在 5 3 8 tl下於空氣中煅燒。 本實施例之産物的X光嫌射形包含在d間隔32.4±2.0 埃處有一甚強之相對強度»及在19.5± 1.0及17.2± 1.0埃 處有弱線。該苯吸附量為41*t涔。因為資施例15之結晶性 材料的苯吸附值為50〆,故本實施例之材料的細孔鼸積確 已滅少。 實施例17 將如實施例4所述之方法製得之煅燒结晶性材料3克加 入於10克水含有0.14克鼸酸絡一水化物之溶液中,使此混 合物在室溫下反應整夜,《量水氣在真空下除去後,在 250TC下於氮氣中乾燥此催化爾5小時,接着再於600TC空 氣中乾嫌9小時,然後將《度降到3501,在一氣化硪中邏 原該試樣30分鐘。 實施例18 將賁施例17之産物在120t:下與在1.91LHSV之1-癸烯 接軀。分離出之低聚合産物,在40*C下黏度為2419簾淹( cS),在lOOt:下則為238cS。計算出之黏度指數為237。 (請先閱讀背而之注意事項#項寫本頁) 裝- 訂- 線- 本紙張尺度逍用中a國家«準(CNS)甲4規格(210X297公釐) 26 81. 6' 丨0,000張(H) Λ 6 _η_6 五、發明説明 (2 7) 實施例19 以如實施例18之方法進行1-癸烯的低聚合,但將反鼷 溫度在1.95 LHSV增為182t。利用蒸籣分離出産物,其黏 度在4〇υ下為197cS,在lOOt:下為27.6cS。《度指數為 178〇 實施例18及19之低聚合産物覆於以本發明方法處理之 结晶性材料上,比用習知技術之Cr/Si〇2催化剤具有更高 之黏度。 (請先閱讀背而之注意事項#堝寫本頁) 經济部中央標準局Μ工消费合作杜印製 81. 6. 10,000張⑻ 本紙張尺度边用中Β國家標準(CNS)肀4規格(210X297公*) 27
Claims (1)
- H3 附 件 第81104088號專利申講案 申讅専利範·修正本 (82年2月1日) 1. 一種改良無櫬,细孔,非成靥之结晶相材料之方法, 該材料在煅燒後舍顬示出在d間隔大於18埃單位處至少 有一波峰及在6.7kpa(50 torr)與251下,每100克該 材料之苯吸附容積大於15克苯,該方法包括在煅燒前 後,將該结晶性材料與包括Μ’X’Y'n之處理組成物接觸 ,其中該組成物之Μ'係選自週期表中IIA, IIIA, IVA, V A , V I A , V I I I A , I Β, I I Β , I I I Β , I V Β , V Β 及 V I Β 者; X’係選自鹵化物,氫化物,Cl-6烷氧化物,Cl-18烷基 ,Cl-18烯基及Cl-8芳基,醋酸塩,Cl-18芳氧化物, 磺酸塩及硝酸塩;Y’係選自X’,胺,膦,硫化物,羰 基及氰基;及n = l- 5。 2. 如申請專利範圃第1項之方法,其中該接觸係在- 70t 至2501之溫度下進行0.1至100小時。 3. 如申請專利範園第1項之方法,其中該接觸係在25t至 1001C之溫度下進行0.1至30小時。 4. 如申請專利範匾第1, 2或3項之方法,其中M'係選自 IVA, VIA, VIIIA, IIIB及 IVB族。 5. 如申請專利範圃第4項之方法,其中Μ ’係選自Ti, Cr, Fe, Co, Ni, B, A1 及 Si〇 6. 如申請專利範_第1, 2或3項之方法,其中X’係遘自鹵 化物,氫化物,Ci-6之烷氧化物及醋酸塩。 7. 如申請專利範圍第6項之方法,其中Y'係選自胺,硫化 1 甲4(210X 297公趑)80. 5ι 5,000張田) H3 物 及 Ci -1 5之烷基。 8 .如 申 請 專 利 範 _第1, 2或 3項之方法, 其 中Μ, X · Y, η係 里 自 醋 m 鉻 f 硝酸鉻 ,四 乙基正矽酸 塩, 四甲基正矽 酸 塩 9 四 乙 氧 化钛, 異丙 氧化鋁,三 -第 二丁 氧化 鋁, 甲 基 二 矽 氨 烷,二 -第二丁氧鋁氧三乙 氧矽 烧, 二乙 基 乙 膦 三 乙 氧 矽烷, 硼酸 CD Sfe Jgm 二甲賭,菜 化二甲基烷基矽 烷 (其中烷基為Ct-M ),氨-硼烷,硼 烧· 四氫 呋喃 ,亞 硫 酸 二 甲 酯 -二溴硼烷及其混合物。 9 .如 甲 請 專 利 範 園第1 , 2或 3項之方法, 其 中該 结晶 相材 料 具 有 >x 下 式 表示之 組成 Μη / q (W aXbYcZdOh), 其中Μ為一或多 涸離 子; η為 除 'Λ Μ代表氧化物外之組成物的電荷; q為Μ之 加權 莫耳 平 均 價 數 η / q為Μ之 奠耳 數或莫耳分 率; V為 —或 多個 二 價 元 素 X為一或多涸三價元素;Y為- -或多個四價 元 素 Z為- -或多個五價元素;a, b, c及d分 別為 W,X ,Y及 Ζ之莫耳分率;h 為1至2 . 5之數; 及(a + b + c + d ) = 1 〇 1 0 .如 甲 請 專 利 範 圍第1 , 2或 3項之方法, 其 中該 结晶 相材 料 具 有 在 無 水 基礎下 之以 下式表示之 組成: Γ RH η / q ( U a X b Yc Z d Oh),其中R為不包含於Μ內 之 缠 有 櫬 材 料 ;r為R 之冥 耳數或莫耳分 率; Μ為- -或 多 個 維 子 η為除Μ代 表氧 化物外之組 成物的電荷; q為Μ 之 加 播 莫 耳 平 均價數 ;η / q為Μ之莫耳 數或莫耳分率;W 為 一 或 多 涸 二 價元素 ;X為一或多個三價 元素 ;丫為 一或 多 個 四 價 元 素 ;Z為- •或多個五價元素; a , b , c 及 d 分 別 為 W , X 9 Y及Z之 奠耳 分率;h為 1至 2 . 5之數; 及 (a + b + C + d )= 1。 甲4(210X297公处)80. S 5,000張(Η) 2
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US07/718,056 US5145816A (en) | 1990-12-10 | 1991-06-20 | Method for functionalizing synthetic mesoporous crystalline material |
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Families Citing this family (60)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5200058A (en) * | 1990-01-25 | 1993-04-06 | Mobil Oil Corp. | Catalytic conversion over modified synthetic mesoporous crystalline material |
US5304363A (en) * | 1990-01-25 | 1994-04-19 | Mobil Oil Corp. | Porous materials |
US5370785A (en) * | 1990-01-25 | 1994-12-06 | Mobil Oil Corp. | Hydrocarbon conversion process employing a porous material |
US5378440A (en) * | 1990-01-25 | 1995-01-03 | Mobil Oil Corp. | Method for separation of substances |
US5308808A (en) * | 1992-02-19 | 1994-05-03 | United States Department Of Energy | Organic or organometallic template mediated clay synthesis |
US5364797A (en) * | 1993-05-20 | 1994-11-15 | Mobil Oil Corp. | Sensor device containing mesoporous crystalline material |
ZA944114B (en) * | 1993-06-17 | 1995-02-07 | Univ Queensland | Kaolin derivatives |
US5348687A (en) * | 1993-11-26 | 1994-09-20 | Mobil Oil Corp. | M41S materials having nonlinear optical properties |
DE4408302C2 (de) * | 1994-03-11 | 1996-04-04 | Zeochem Kft | Verfahren zur Herstellung und Verwendung eines festen Verbundproduktes zur Wasserbehandlung |
US5560748A (en) * | 1994-06-10 | 1996-10-01 | The Procter & Gamble Company | Detergent compositions comprising large pore size redox catalysts |
DE19515932C2 (de) * | 1995-05-02 | 2000-09-21 | Feistel Gmbh Industrievertretu | Verwendung eines Zeolith-Verbundprodukts |
US6054052A (en) * | 1995-12-14 | 2000-04-25 | Mobil Oil Corporation | Selective sorption of organics by metal-containing M41S |
DE19543638A1 (de) * | 1995-11-23 | 1997-05-28 | Basf Ag | Mesoporöse Molekularsiebe |
US6284696B1 (en) * | 1996-06-07 | 2001-09-04 | Asahi Kasei Kogyo Kabushiki Kaisha | Mesopore molecular sieve and process for the production thereof |
US5718878A (en) * | 1996-07-12 | 1998-02-17 | Akzo Nobel N.V. | Mesoporous titania and process for its preparation |
US5922299A (en) | 1996-11-26 | 1999-07-13 | Battelle Memorial Institute | Mesoporous-silica films, fibers, and powders by evaporation |
WO1998046353A1 (en) | 1997-04-15 | 1998-10-22 | Massachusetts Institute Of Technology | Synthesis and application of vapor grafted porous materials |
US5965474A (en) * | 1997-04-29 | 1999-10-12 | Mobil Oil Corporation | FCC metal traps based on ultra large pore crystalline material |
CN1073887C (zh) * | 1997-08-08 | 2001-10-31 | 北京燕化石油化工股份有限公司化工二厂 | 烷基化制乙苯催化剂、其制法、烷基化制乙苯新工艺 |
US6331500B1 (en) * | 1997-08-25 | 2001-12-18 | California Institute Of Technology | Functionalized molecular sieves |
DE19745905A1 (de) * | 1997-10-17 | 1999-04-22 | Hoechst Ag | Trägerkatalysatoren mit hoher Sinterstabilität und Verfahren zu deren Herstellung |
US6326326B1 (en) * | 1998-02-06 | 2001-12-04 | Battelle Memorial Institute | Surface functionalized mesoporous material and method of making same |
US5925330A (en) * | 1998-02-13 | 1999-07-20 | Mobil Oil Corporation | Method of m41s functionalization of potentially catalytic heteroatom centers into as-synthesized m41s with concomitant surfactant extraction |
US6319872B1 (en) * | 1998-08-20 | 2001-11-20 | Conoco Inc | Fischer-Tropsch processes using catalysts on mesoporous supports |
US6329017B1 (en) | 1998-12-23 | 2001-12-11 | Battelle Memorial Institute | Mesoporous silica film from a solution containing a surfactant and methods of making same |
US6383466B1 (en) | 1998-12-28 | 2002-05-07 | Battelle Memorial Institute | Method of dehydroxylating a hydroxylated material and method of making a mesoporous film |
US6096469A (en) * | 1999-05-18 | 2000-08-01 | 3M Innovative Properties Company | Ink receptor media suitable for inkjet printing |
WO2001014060A2 (en) | 1999-08-25 | 2001-03-01 | Massachusetts Institute Of Technology | Surface-confined catalytic compositions |
US6930219B2 (en) * | 1999-09-07 | 2005-08-16 | Abb Lummus Global Inc. | Mesoporous material with active metals |
US20040089238A1 (en) * | 1999-10-04 | 2004-05-13 | Jerome Birnbaum | Vacuum/gas phase reactor for dehydroxylation and alkylation of porous silica |
FR2806643B1 (fr) | 2000-03-27 | 2002-05-03 | Ceca Sa | Methode de separation de molecules en phase gaz par adsorption au moyen d'adsorbants inorganiques solides agglomeres a distribution mesoporeuse etroite et calibree |
US6585863B2 (en) | 2000-08-08 | 2003-07-01 | Procter & Gamble Company | Photocatalytic degradation of organic compounds |
AUPR113700A0 (en) * | 2000-10-31 | 2000-11-23 | Australian Nuclear Science & Technology Organisation | Transition metal oxide compositions |
US6960551B2 (en) * | 2002-08-23 | 2005-11-01 | Exxonmobil Research And Engineering Company | Functionalized periodic mesoporous materials, their synthesis and use |
US6812373B2 (en) * | 2002-12-12 | 2004-11-02 | Exxonmobil Chemical Patents Inc. | Modified metalloaluminophosphate molecular sieves |
US6906233B2 (en) * | 2002-12-12 | 2005-06-14 | Exxon Mobil Chemical Patents Inc. | Modified metalloaluminophosphate molecular sieves |
US7563451B2 (en) | 2003-07-22 | 2009-07-21 | Iowa State University Research Foundation, Inc. | Capped mesoporous silicates |
US20060018966A1 (en) * | 2003-07-22 | 2006-01-26 | Lin Victor S | Antimicrobial mesoporous silica nanoparticles |
US20050033102A1 (en) * | 2003-08-06 | 2005-02-10 | Randolph Bruce B. | Supported ionic liquid and the use thereof in the disproportionation of isopentane |
US20050176978A1 (en) * | 2003-12-15 | 2005-08-11 | Verkade John G. | Immobilized iminophosphatranes useful for transesterification |
US7151073B2 (en) * | 2004-01-16 | 2006-12-19 | Exxonmobil Chemical Patents Inc. | Mesoporous catalyst support, a catalyst system, and method of making and using same for olefin polymerization |
US7919659B2 (en) | 2004-07-09 | 2011-04-05 | Asahi Kasei Chemicals Corporation | Catalyst for cycloolefin production and process for production |
JP2006069877A (ja) * | 2004-09-06 | 2006-03-16 | Marukatsu Sangyo Kk | メソポーラスチタニア |
US7838461B2 (en) | 2004-11-01 | 2010-11-23 | Asahi Kasei Kabushiki Kaisha | Catalyst for exhaust gas purification |
KR101098495B1 (ko) | 2005-08-15 | 2011-12-26 | 상하이 리서치 인스티튜트 오브 페트로케미칼 테크놀로지 시노펙 | 톨루엔 형태 선택성 알킬화반응에 의한 파라-자일렌 제조용촉매의 제조방법 |
US7678955B2 (en) * | 2005-10-13 | 2010-03-16 | Exxonmobil Chemical Patents Inc | Porous composite materials having micro and meso/macroporosity |
JP2007222842A (ja) * | 2006-02-27 | 2007-09-06 | Asahi Kasei Corp | 排NOx浄化用触媒及びその担体 |
US8383079B2 (en) * | 2006-04-17 | 2013-02-26 | Exxonmobil Chemical Patents Inc. | Molecular sieves having micro and mesoporosity, their synthesis and their use in the organic conversion reactions |
US8647644B1 (en) | 2006-04-19 | 2014-02-11 | Iowa State University Research Foundation, Inc. | Methods of using capped mesoporous silicates |
US20090191458A1 (en) * | 2007-07-23 | 2009-07-30 | Matsushita Electric Industrial Co., Ltd. | Porous network negative electrodes for non-aqueous electrolyte secondary battery |
TWI435765B (zh) * | 2007-12-27 | 2014-05-01 | Exxonmobil Res & Eng Co | 芳族氫化作用之催化劑及方法 |
CA2718470A1 (en) * | 2008-03-21 | 2009-09-24 | Queen's University At Kingston | Multi-channel electrospray emitter |
KR100945020B1 (ko) * | 2008-03-27 | 2010-03-05 | 한국원자력연구원 | 흡착제, 이의 제조방법 및 이를 이용한 스트론튬/이트륨발생기 |
US20100087610A1 (en) * | 2008-10-06 | 2010-04-08 | Vaughn Stephen N | Method Of Preparing And Using A Molecular Sieve |
JP5426869B2 (ja) * | 2008-11-19 | 2014-02-26 | パナソニック株式会社 | メソポーラスシリカ微粒子の製造方法、メソポーラスシリカ微粒子含有組成物、及びメソポーラスシリカ微粒子含有成型物 |
CN101804324B (zh) * | 2010-04-16 | 2012-06-20 | 南京大学 | 一种对废水中氨氮具有高选择性的改性分子筛及其制备方法 |
JP2010265174A (ja) * | 2010-07-27 | 2010-11-25 | Asahi Kasei Chemicals Corp | 変性メソポーラス酸化物 |
JP6196035B2 (ja) * | 2012-12-21 | 2017-09-13 | 千代田化工建設株式会社 | 非水溶性物質を含む水の処理方法 |
LU92783B1 (en) * | 2015-07-22 | 2017-01-31 | Luxembourg Inst Of Science And Tech (List) | Highly aminated self-assembling fuctionalized Mesoporous Silicia Nanoparticles and methods of synthesis |
EP3517500A1 (en) | 2018-01-24 | 2019-07-31 | Technische Universität Berlin | A method for obtaining mesoporous silica particles with surface functionalisation |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3274120A (en) * | 1964-02-20 | 1966-09-20 | Cabot Corp | Catalyst composition having increased hydroxyl groups bound thereto and method for producing same |
US3725302A (en) * | 1969-06-17 | 1973-04-03 | Texaco Inc | Silanized crystalline alumino-silicate |
US3698157A (en) * | 1971-06-01 | 1972-10-17 | Mobil Oil Corp | Separation of mixtures with modified zeolites |
CA1051855A (en) * | 1974-10-07 | 1979-04-03 | David E.W. Vaughan | Zeolite vk-2 |
ZA794221B (en) * | 1978-09-05 | 1981-03-25 | British Petroleum Co | Process for the preparation of a functionalised solid product |
US4292205A (en) * | 1979-07-20 | 1981-09-29 | Mobil Oil Corporation | Ion exchange and impregnation of catalysts |
DE3117135A1 (de) * | 1981-04-30 | 1982-11-18 | Bayer Ag, 5090 Leverkusen | Kristallines alumosilicat, verfahren zu dessen herstellung sowie dessen verwendung zur katalytischen umwandlung von methanol und/oder dimethylether in kohlenwasserstoffe |
US4390414A (en) * | 1981-12-16 | 1983-06-28 | Exxon Research And Engineering Co. | Selective dewaxing of hydrocarbon oil using surface-modified zeolites |
US4954325A (en) * | 1986-07-29 | 1990-09-04 | Mobil Oil Corp. | Composition of synthetic porous crystalline material, its synthesis and use |
JPH02500434A (ja) * | 1986-08-22 | 1990-02-15 | リサーチ コーポレーション リミテッド | ゼオライトの改良 |
US4933161A (en) * | 1987-02-04 | 1990-06-12 | Exxon Research And Engineering Company | Tin substitution into zeolite frameworks |
JPH0761858B2 (ja) * | 1987-03-19 | 1995-07-05 | 日揮株式会社 | ゼオライト細孔径の精密制御法 |
EP0321177B1 (en) * | 1987-12-15 | 1994-08-03 | Uop | Substitution of Cr and/or Sn in place of A1 in the framework of molecular sieve via treatment with fluoride salts |
-
1991
- 1991-06-20 US US07/718,056 patent/US5145816A/en not_active Expired - Lifetime
-
1992
- 1992-05-19 EP EP92304525A patent/EP0533312B1/en not_active Expired - Lifetime
- 1992-05-19 DE DE69225183T patent/DE69225183T2/de not_active Expired - Fee Related
- 1992-05-20 AU AU16396/92A patent/AU648166B2/en not_active Ceased
- 1992-05-26 TW TW081104088A patent/TW204329B/zh active
- 1992-05-27 CA CA002069722A patent/CA2069722C/en not_active Expired - Fee Related
- 1992-06-17 KR KR1019920010496A patent/KR100205979B1/ko not_active IP Right Cessation
- 1992-06-19 JP JP16080492A patent/JP3443428B2/ja not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
AU1639692A (en) | 1992-12-24 |
JP3443428B2 (ja) | 2003-09-02 |
JPH05254827A (ja) | 1993-10-05 |
DE69225183D1 (de) | 1998-05-28 |
US5145816A (en) | 1992-09-08 |
CA2069722A1 (en) | 1992-12-21 |
AU648166B2 (en) | 1994-04-14 |
CA2069722C (en) | 2002-12-17 |
EP0533312A1 (en) | 1993-03-24 |
KR930000161A (ko) | 1993-01-15 |
DE69225183T2 (de) | 1998-08-13 |
KR100205979B1 (ko) | 1999-07-01 |
EP0533312B1 (en) | 1998-04-22 |
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