CN1774398A - 高活性小晶体zsm-12 - Google Patents
高活性小晶体zsm-12 Download PDFInfo
- Publication number
- CN1774398A CN1774398A CNA2003801051636A CN200380105163A CN1774398A CN 1774398 A CN1774398 A CN 1774398A CN A2003801051636 A CNA2003801051636 A CN A2003801051636A CN 200380105163 A CN200380105163 A CN 200380105163A CN 1774398 A CN1774398 A CN 1774398A
- Authority
- CN
- China
- Prior art keywords
- zsm
- crystalline material
- porous crystalline
- temperature
- mixture
- 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.)
- Granted
Links
- 239000013078 crystal Substances 0.000 title claims abstract description 28
- 230000000694 effects Effects 0.000 title description 7
- 239000000203 mixture Substances 0.000 claims abstract description 46
- 239000000463 material Substances 0.000 claims abstract description 38
- 239000002178 crystalline material Substances 0.000 claims abstract description 22
- AUHZEENZYGFFBQ-UHFFFAOYSA-N mesitylene Substances CC1=CC(C)=CC(C)=C1 AUHZEENZYGFFBQ-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000009792 diffusion process Methods 0.000 claims abstract description 8
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 31
- 238000000034 method Methods 0.000 claims description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 238000006243 chemical reaction Methods 0.000 claims description 19
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 18
- 150000001875 compounds Chemical class 0.000 claims description 14
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 10
- 239000001257 hydrogen Substances 0.000 claims description 10
- 239000011734 sodium Substances 0.000 claims description 10
- 229930195733 hydrocarbon Natural products 0.000 claims description 9
- 150000002430 hydrocarbons Chemical class 0.000 claims description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 8
- 150000002500 ions Chemical class 0.000 claims description 8
- 239000004215 Carbon black (E152) Substances 0.000 claims description 7
- 239000011541 reaction mixture Substances 0.000 claims description 7
- 229910052782 aluminium Inorganic materials 0.000 claims description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 6
- SEACXNRNJAXIBM-UHFFFAOYSA-N triethyl(methyl)azanium Chemical compound CC[N+](C)(CC)CC SEACXNRNJAXIBM-UHFFFAOYSA-N 0.000 claims description 6
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 5
- 239000002808 molecular sieve Substances 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 229910052710 silicon Inorganic materials 0.000 claims description 5
- 239000010703 silicon Substances 0.000 claims description 5
- 229910052708 sodium Inorganic materials 0.000 claims description 5
- 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 5
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 4
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 4
- 239000004411 aluminium Substances 0.000 claims description 4
- 229910052728 basic metal Inorganic materials 0.000 claims description 4
- 150000003818 basic metals Chemical class 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 3
- 125000000217 alkyl group Chemical group 0.000 claims 2
- 238000012216 screening Methods 0.000 claims 1
- 125000001827 mesitylenyl group Chemical group [H]C1=C(C(*)=C(C([H])=C1C([H])([H])[H])C([H])([H])[H])C([H])([H])[H] 0.000 abstract description 9
- 229910004298 SiO 2 Inorganic materials 0.000 description 34
- 229920002994 synthetic fiber Polymers 0.000 description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 239000008367 deionised water Substances 0.000 description 12
- 229910021641 deionized water Inorganic materials 0.000 description 12
- 239000000047 product Substances 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 10
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 10
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 9
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 238000001035 drying Methods 0.000 description 8
- 238000005342 ion exchange Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 238000003756 stirring Methods 0.000 description 8
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 7
- 229910021536 Zeolite Inorganic materials 0.000 description 7
- 239000004927 clay Substances 0.000 description 7
- 230000009466 transformation Effects 0.000 description 7
- 239000010457 zeolite Substances 0.000 description 7
- 230000003197 catalytic effect Effects 0.000 description 6
- 230000008859 change Effects 0.000 description 6
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 6
- 230000009257 reactivity Effects 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 5
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N 1,2-diethylbenzene Chemical compound CCC1=CC=CC=C1CC KVNYFPKFSJIPBJ-UHFFFAOYSA-N 0.000 description 4
- QPUYECUOLPXSFR-UHFFFAOYSA-N 1-methylnaphthalene Chemical compound C1=CC=C2C(C)=CC=CC2=C1 QPUYECUOLPXSFR-UHFFFAOYSA-N 0.000 description 4
- 239000005995 Aluminium silicate Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 4
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 235000012211 aluminium silicate Nutrition 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- PQNFLJBBNBOBRQ-UHFFFAOYSA-N indane Chemical compound C1=CC=C2CCCC2=C1 PQNFLJBBNBOBRQ-UHFFFAOYSA-N 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 229910052697 platinum Inorganic materials 0.000 description 4
- UOHMMEJUHBCKEE-UHFFFAOYSA-N prehnitene Chemical compound CC1=CC=C(C)C(C)=C1C UOHMMEJUHBCKEE-UHFFFAOYSA-N 0.000 description 4
- ODLMAHJVESYWTB-UHFFFAOYSA-N propylbenzene Chemical compound CCCC1=CC=CC=C1 ODLMAHJVESYWTB-UHFFFAOYSA-N 0.000 description 4
- 229910052702 rhenium Inorganic materials 0.000 description 4
- YTZKOQUCBOVLHL-UHFFFAOYSA-N tert-butylbenzene Chemical compound CC(C)(C)C1=CC=CC=C1 YTZKOQUCBOVLHL-UHFFFAOYSA-N 0.000 description 4
- WSWCOQWTEOXDQX-MQQKCMAXSA-M (E,E)-sorbate Chemical compound C\C=C\C=C\C([O-])=O WSWCOQWTEOXDQX-MQQKCMAXSA-M 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 3
- 238000002441 X-ray diffraction Methods 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- ZUSFORRWERTRDS-UHFFFAOYSA-N chloromethane;n,n-diethylethanamine Chemical compound ClC.CCN(CC)CC ZUSFORRWERTRDS-UHFFFAOYSA-N 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 229940075554 sorbate Drugs 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- HYFLWBNQFMXCPA-UHFFFAOYSA-N 1-ethyl-2-methylbenzene Chemical compound CCC1=CC=CC=C1C HYFLWBNQFMXCPA-UHFFFAOYSA-N 0.000 description 2
- FIPKSKMDTAQBDJ-UHFFFAOYSA-N 1-methyl-2,3-dihydro-1h-indene Chemical compound C1=CC=C2C(C)CCC2=C1 FIPKSKMDTAQBDJ-UHFFFAOYSA-N 0.000 description 2
- YRNMHHHHSMCMHJ-UHFFFAOYSA-N 2-(diethylamino)ethyl-triethylazanium Chemical compound CCN(CC)CC[N+](CC)(CC)CC YRNMHHHHSMCMHJ-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 2
- GYHNNYVSQQEPJS-UHFFFAOYSA-N Gallium Chemical compound [Ga] GYHNNYVSQQEPJS-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 2
- 229910021502 aluminium hydroxide Inorganic materials 0.000 description 2
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- ZSIQJIWKELUFRJ-UHFFFAOYSA-N azepane Chemical compound C1CCCNCC1 ZSIQJIWKELUFRJ-UHFFFAOYSA-N 0.000 description 2
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 238000002447 crystallographic data Methods 0.000 description 2
- RWGFKTVRMDUZSP-UHFFFAOYSA-N cumene Chemical compound CC(C)C1=CC=CC=C1 RWGFKTVRMDUZSP-UHFFFAOYSA-N 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 229910052733 gallium Inorganic materials 0.000 description 2
- 229910052732 germanium Inorganic materials 0.000 description 2
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 2
- 230000026030 halogenation Effects 0.000 description 2
- 238000005658 halogenation reaction Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
- 230000006911 nucleation Effects 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 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
- 229910001388 sodium aluminate Inorganic materials 0.000 description 2
- 239000002594 sorbent Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CBXCPBUEXACCNR-UHFFFAOYSA-N tetraethylammonium Chemical compound CC[N+](CC)(CC)CC CBXCPBUEXACCNR-UHFFFAOYSA-N 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 1
- SDGKUVSVPIIUCF-UHFFFAOYSA-N 2,6-dimethylpiperidine Chemical compound CC1CCCC(C)N1 SDGKUVSVPIIUCF-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- RWRDLPDLKQPQOW-UHFFFAOYSA-O Pyrrolidinium ion Chemical compound C1CC[NH2+]C1 RWRDLPDLKQPQOW-UHFFFAOYSA-O 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- HPTYUNKZVDYXLP-UHFFFAOYSA-N aluminum;trihydroxy(trihydroxysilyloxy)silane;hydrate Chemical compound O.[Al].[Al].O[Si](O)(O)O[Si](O)(O)O HPTYUNKZVDYXLP-UHFFFAOYSA-N 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000008901 benefit Effects 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
- LTPBRCUWZOMYOC-UHFFFAOYSA-N beryllium oxide Inorganic materials O=[Be] LTPBRCUWZOMYOC-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- OCKPCBLVNKHBMX-UHFFFAOYSA-N butylbenzene Chemical compound CCCCC1=CC=CC=C1 OCKPCBLVNKHBMX-UHFFFAOYSA-N 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- RBUJTRYJXATERJ-UHFFFAOYSA-N dibenzyl(diethyl)azanium Chemical compound C=1C=CC=CC=1C[N+](CC)(CC)CC1=CC=CC=C1 RBUJTRYJXATERJ-UHFFFAOYSA-N 0.000 description 1
- 229910001649 dickite Inorganic materials 0.000 description 1
- ZJHQDSMOYNLVLX-UHFFFAOYSA-N diethyl(dimethyl)azanium Chemical compound CC[N+](C)(C)CC ZJHQDSMOYNLVLX-UHFFFAOYSA-N 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000021321 essential mineral Nutrition 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 229910052621 halloysite Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- APFVFJFRJDLVQX-UHFFFAOYSA-N indium atom Chemical compound [In] APFVFJFRJDLVQX-UHFFFAOYSA-N 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-M iodide Chemical compound [I-] XMBWDFGMSWQBCA-UHFFFAOYSA-M 0.000 description 1
- 229910052622 kaolinite Inorganic materials 0.000 description 1
- JCCNYMKQOSZNPW-UHFFFAOYSA-N loratadine Chemical compound C1CN(C(=O)OCC)CCC1=C1C2=NC=CC=C2CCC2=CC(Cl)=CC=C21 JCCNYMKQOSZNPW-UHFFFAOYSA-N 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- CLSUSRZJUQMOHH-UHFFFAOYSA-L platinum dichloride Chemical compound Cl[Pt]Cl CLSUSRZJUQMOHH-UHFFFAOYSA-L 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 230000002285 radioactive effect Effects 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 229910019655 synthetic inorganic crystalline material Inorganic materials 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
- HWCKGOZZJDHMNC-UHFFFAOYSA-M tetraethylammonium bromide Chemical compound [Br-].CC[N+](CC)(CC)CC HWCKGOZZJDHMNC-UHFFFAOYSA-M 0.000 description 1
- QEMXHQIAXOOASZ-UHFFFAOYSA-N tetramethylammonium Chemical compound C[N+](C)(C)C QEMXHQIAXOOASZ-UHFFFAOYSA-N 0.000 description 1
- ZMANZCXQSJIPKH-UHFFFAOYSA-O triethylammonium ion Chemical compound CC[NH+](CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-O 0.000 description 1
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 1
- -1 trimethylene ions Chemical class 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- 230000004304 visual acuity Effects 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
- C07C6/08—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond
- C07C6/12—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring
- C07C6/126—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions by conversion at a saturated carbon-to-carbon bond of exclusively hydrocarbons containing a six-membered aromatic ring of more than one hydrocarbon
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/7034—MTW-type, e.g. ZSM-12, NU-13, TPZ-12 or Theta-3
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
-
- 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
- C01B39/42—Type ZSM-12
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
- C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
- C10G45/64—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/42—Addition of matrix or binder particles
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/80—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with zinc, cadmium or mercury
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/80—Mixtures of different zeolites
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/30—Aromatics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S423/00—Chemistry of inorganic compounds
- Y10S423/33—MTW, e.g. ZSM-12, NU-13, CZH-5, TPZ-3
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Crystallography & Structural Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Porous Artificial Stone Or Porous Ceramic Products (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
一种具有ZSM-12骨架结构和符合以下摩尔关系式的组成的多孔结晶材料:X2O3:(n)YO2,其中X是三价元素,Y是四价元素,n小于60,该材料的平均晶体尺寸小于0.1微米,和该材料在100℃的温度和2乇的均三甲苯压力下测量时对于均三甲苯的扩散参数至少为1000×10-6秒-1。
Description
发明领域
本发明涉及一种高活性小晶体ZSM-12、它的合成以及它在催化过程中的应用,特别是在C9+芳香烃转化成二甲苯的过程中的应用。
发明背景
ZSM-12及其在四甲铵或者四乙铵定向剂存在下的传统制备方法已在美国专利NO.3832449中有教导,在这此引入作为参考。ZSM-12独特的X射线衍射图样使其与其它已知的结晶材料区别开来。
美国专利NO.4391785公开从一种反应混合物合成ZSM-12的方法,该混合物包含作为定向剂的选自二甲基卤化吡啶鎓与二甲基卤化吡咯烷鎓盐中的化合物。
美国专利NO.4452769和4537758公开了从包含甲基三乙基铵离子作为定向剂的反应混合物合成ZSM-12的方法。可是,这些专利基本上是生产高SiO2/Al2O3比例形式的ZSM-12,在‘769专利中该比例高于80而在‘758专利中该比例高于200。还有,在利用甲基三乙基铵离子作为定向剂的‘769专利中提出的优点之一是大晶体尺寸的材料的生产。
其它用于合成ZSM-12的有机定向剂包括双(二甲基哌啶鎓)三亚甲基离子(参见US4539193),苯甲基三乙基铵离子(参见US4552738),二苄基二乙基铵离子(参见EP-A-167232),二甲基二乙基铵离子(参见US4552739),苄基三甲基铵离子(参见US4585637),双(N-甲基吡啶基)ethylinium离子(参见US45852746),六亚甲基亚胺(US5021141)和双(甲基吡咯烷鎓盐)-diquat-n,其中n=4,5或6(参见US5192521)。
尽管受着各种变化因素如反应混合物的二氧化硅/氧化铝摩尔比率,温度和搅拌的影响,合成沸石例如ZSM-12的晶体形态主要由用于结晶的定向剂的选择来控制。例如对于ZSM-12,利用苯甲基三甲基铵定向剂时得到针状晶体,在四乙基铵盐存在时得到稻谷状晶体,利用六亚甲基亚胺定向剂产生六方形片晶束。
从提高活性和稳定性的观点来说沸石晶体形态的控制是非常重要的。对于催化应用而言,要得到高活性和稳定性,小晶体尺寸总是期望的,因为小晶体材料具有更大的表面积,从而有较短的扩散程。同时由于沸石的活性也与沸石骨架中的铝原子有关,沸石的SiO2/Al2O3比例越低,沸石的酸性越高。迄今为止,大多数ZSM-12的合成路线是要么得到小晶体材料要么得到低SiO2/Al2O3比例的材料。然而一般很难合成既有小晶体尺寸又有低SiO2/Al2O3比例的高纯度ZSM-12。
本发明的目的是提供一种高活性小晶体形式的ZSM-12,其在C9+芳香烃转化成二甲苯的过程中表现出增强的活性。
可以认识到,尽管ZSM-12正常以铝硅酸盐形式合成,骨架铝能被其它三价元素部分或完全地代替,例如硼、铁和/或镓;骨架硅也能被其它四价元素部分或完全地代替,例如锗。
发明概述
本发明一方面涉及一种具有ZSM-12骨架结构和符合以下摩尔关系式的组成的多孔结晶材料:
X2O3:(n)YO2
其中X是三价元素,Y是四价元素,和n小于60,
其中材料的平均晶体尺寸小于0.1微米,和
其中该材料在100℃的温度和2乇的均三甲苯压力下测量时对于均三甲苯的扩散参数至少为1000×10-6秒-1。
优选,n是20到小于60。
优选,X是铝和Y是硅。
优选,材料的α值超过300。
在再一方面,本发明涉及合成本发明的所述一方面的ZSM-12多孔结晶材料的方法,包括以下步骤:
(a)制备能形成所述材料的混合物,所述混合物包含碱金属或碱土金属(M)源、三价元素(X)的氧化物、四价元素(Y)的氧化物、氢氧根离子(OH-)、水和甲基三乙基铵阳离子(R),其中所述混合物具有以下摩尔比率范围内的组成:
YO2/X2O3<100
H2O/YO2=10-100
OH-/YO2=0.1-0.6
M/YO2=0.1-0.6
R/YO2=0.1-0.6,
(b)保持所述混合物在足够的条件下,直到形成所述材料的晶体为止;和
(c)从步骤(ii)回收所述晶体材料。
优选,所述反应混合物具有以下摩尔比率范围内的组成:
YO2/X2O3=40-80
H2O/YO2=15-40
OH-/YO2=0.15-0.4
M/YO2=0.15-0.4
R/YO2=0.15-0.4
优选,所述条件包括温度为140℃-170℃。
优选,M是钠。
附图说明
图1到图3分别是实施例1到3所合成的产品的扫描电子显微照片(SEM)。
图4是实施例7所合成的产品的扫描电子显微照片(SEM)。
图5是实施例1到7的氢形式的ZSM-12产品中SiO2/Al2O3比例对α活性的曲线。
实施方案的详述
根据本发明的ZSM-12具有由下表1所列X射线衍射线表征的X射线衍射图样:
表1
D-间距(埃) | 相对强度[100×I/I0] |
11.9±0.210.1±0.24.76±0.14.29±0.083.98±0.083.87±0.073.49±0.073.38±0.073.20±0.063.05±0.052.54±0.03 | mmwvsmvswmwww |
利用铜K-α放射线的Scintag衍射仪收集X射线衍射数据。通过在2θ的0.02度逐步扫描记录衍射数据,其中θ是布勒格角,每步的计时为1秒。晶面间距d以埃计(),射线的相对强度I/I0,用轮廓拟合方法(profile fitting routine)(或二阶导数算法)得出,其中I0是最强线的强度的百分之一。强度未对于洛伦兹和极化效应加以校正。相对强度以符号给出,符号vs=非常强(75-100),s=强(50-74),m=中(25-49)和w=弱(0-24)。可以理解,对于这一样品所列出的作为单线的衍射数据可以由许多重叠的线构成,而这些重叠的线在某些条件下,例如微晶大小的差异、非常高的实验分辨率或结晶学变化,会表现为分辨或部分分辨的线。典型地,结晶学变化可以包括晶胞参数的微小变化和/或晶体对称性的变化,但没有晶体结构的拓扑学变化。由于阳离子含量、骨架组成、孔隙充填的性质和程度、热和/或水热历史,也引起这些微小的效应,包括相对强度的改变。
本发明的晶体材料ZSM-12具有符合以下摩尔关系式的组成:
X2O3:(n)YO2
其中X是三价元素,例如铝、硼、铁、铟和/或镓,优选铝;Y是四价元素,例如硅、锡和/或锗。优选硅;和n小于60,优选从20到小于60。在它所合成的形式中,在无水的基础上并根据每n摩尔YO2的各种氧化物的摩尔数,本发明的结晶材料具有以下关系式:
(0.01-2)M2O:(0.01-2)R2O:X2O3:(n)YO2
其中M是碱金属或碱土金属,优选钠,R是甲基三乙基铵阳离子。由于它们在结晶期间的存在,M和R组分与该材料相结合,并能容易地通过以下更详细叙述的结晶后方法去除。
本发明的ZSM-12具有小于0.1微米的材料平均晶体尺寸,优选大约0.05微米,并具有在100℃的温度和2乇均三甲苯压力下测量时至少1000×10-6秒-1,和优选至少2000×10-6sec-1的对均三甲苯的扩散参数(D/r2)。
正如在此使用的,一种特定多孔结晶材料的扩散参数定义为D/r2×106,其中D是扩散系数(cm2/sec)和r是晶体半径(cm)。所要求的扩散参数是从吸着测量法获得的,假设平面片模型描述扩散过程。因此对于一个给定的吸着物负荷Q,Q/Q∞的值在数学上与(Dt/r2)1/2相关,其中Q∞是平衡吸着物负荷,t是达到吸着物负荷Q所需要的时间(sec)。平面片模型的图示解法已由J.Grank在“The Mathematics ofDiffusion”,Oxford University Press,Ely House,London,1967中给出。
本发明的ZSM-12优选具有至少150的α值,更优选至少300。α值测试是催化剂的裂化活性的量度,并描叙在美国专利NO.3354078和在Journal of Catalysis,Vol.4,p.527(1965);Vol.6,p.278(1966);和Vol.61,p.395(1980)中,在此引入该描述作为参考。在此用到的测试的实验条件包括538℃的恒温和可变的流动速率,如在Journal of Catalysis,Vol.61,p.395中所详细描述。
本发明的ZSM-12从一种合成混和物生产,该合成混合物包含碱金属或碱土金属(M)阳离子(一般为钠)的源物质;三价元素(X)的氧化物,一般为氧化铝;四价元素(Y)的氧化物,一般为氧化硅;甲基三乙基铵离子(R),一般作为碘化物盐存在,氢氧根离子和水。该合成混合物具有如下的按氧化物的摩尔比率表达的组成:
组分 | 有用的 | 优选的 |
YO2/X2O3 | 20-100 | 40-80 |
H2O/YO2 | 10-100 | 15-40 |
OH-/YO2 | 0.1-0.6 | 0.15-0.4 |
R/YO2 | 0.1-0.6 | 0.15-0.4 |
M/YO2 | 0.1-0.6 | 0.15-0.4 |
本发明的合成方法可以在加入或没有加入成核用种晶的情况下进行。在一个优选方案中,反应混合物含有0.05-5wt%的ZSM-12的成核用种晶。
结晶既可以在搅拌也可以在静态条件下进行,优选在搅拌条件下,在170℃或170℃以下和优选140-160℃的较低温度下进行。优选结晶进行48-500小时,随后所得ZSM-12晶体从母液中分离并回收。
在它的合成形式中,本发明的ZSM-12包含作为定向剂的有机材料,并在用作催化剂或吸附剂之前,此合成材料一般需要处理以除去部分或全部有机成分。这可以通过在250℃-550℃的温度下加热合成材料1-48小时来实现。
至所希望的程度,所合成的材料中的原始钠和/或钾阳离子可以根据本领域熟知的技术,通过与其它阳离子的离子交换,至少一部分地被取代。优选取代用阳离子包括金属离子、氢离子、氢前体例如铵离子和它们的混合物。特别优选的阳离子是为了特定烃转化反应而确定催化活性的那些。它们包括氢、稀土金属和元素周期表IIA,IIIA,IVA,VA,IB,IIB,IIIB,IVB,VB,VIB,VIIB和VIII族的金属。
本发明的结晶材料当在有机化合物转化过程中用作吸附剂或用作催化剂时应该被脱水,至少部分脱水。这可以通过在常压、低于大气压或高于大气压下在诸如空气或氮气之类的气氛中加热到200℃-370℃范围内的温度保持30分钟到48小时来实现。脱水过程也可以在室温下仅仅将ZSM-12在真空下放置来进行,但是要得到充分的脱水效果需要更长的时间。
根据此方法获得的合成ZSM-12晶体能够以所合成的形式,氢形式或另一种单价或多价阳离子形式使用。在要发挥加氢-脱氢功能的情况下,它也能够与加氢用组分如钨、钒、钼、铼、镍、钴、铬、锰或贵金属如铂或钯紧密相结合使用。此类组分能够交换到组合物中,浸渍在其中或与其实现物理紧密掺混。此类组分能够浸渍在ZSM-12之中或之上,例如,对于铂,通过用含铂金属的离子处理该材料。用于此目的的合适铂化合物包括氯铂酸、氯化亚铂和各种含有铂胺络合物的化合物。金属的结合物和有关它们的引入的方法也能够使用。
当用作催化剂时,希望将本发明的ZSM-12与另外一种耐受用于某些有机转化过程中的温度和其它条件的材料相混合。该基体材料包括活性和非活性材料和合成或天然沸石以及无机材料如粘土、硅石和/或金属氧化物例如氧化铝、二氧化钛和/或氧化锆。后者可以是自然形成的或是包括硅石和金属氧化物的混合物的凝胶状沉淀物、溶胶或凝胶的形式。与ZSM-12一起,即与其相结合,的材料的使用(该材料是活性的)可以增强催化剂在某些有机转化过程中的转化率和/或选择性。非活性的材料适合作为稀释剂来控制在给定过程中的转化量以便经济地和有序地获得产品,无需利用其它方法来控制反应速率。结晶的催化材料已经常地引入天然粘土中,如膨润土和高岭土。这些材料即粘土、氧化物等部分地作为催化剂的粘结剂。希望提供一种具有良好的压碎强度的催化剂,因为在炼油厂中,催化剂经常受到粗糙的处置,倾向于使得催化剂破裂成粉末状材料而在处理中引起问题。
能与所合成的结晶材料复合的天然粘土包括蒙脱土和高岭土类,该高岭土类包括变膨润土和通常已知为Dixie,McNamee,Georgia和Florida粘土的高岭土,或其中主要矿物成分为多水高岭土、高岭石、地开石、珍珠陶土或蠕陶土的其它粘土。此类粘土能以最初开采出来的原始状态利用或初步进行煅烧、酸处理或化学改性后利用。
除了前述材料之外,本发明催化剂也能与多孔基体材料如硅石-氧化铝,硅石-氧化镁,硅石-氧化锆,硅石-二氧化钍,硅石-氧化铍,硅石-二氧化钛,以及三元组合物如硅石-氧化铝-二氧化钍,硅石-氧化铝-氧化锆,硅石-氧化铝-氧化镁和硅石-氧化镁-氧化锆进行复合。基体材料可以是共凝胶形式。也可以使用这些组分的混合物。
细分散的结晶材料和基体材料的相对比例将随着在相当于复合材料的约1wt%到约90wt%,更通常地约2wt%-约50wt%范围内的结晶材料的含量而较宽地变化。
根据本发明的铝硅酸盐ZSM-12可用作在有机化合物(尤其是烃)转化反应中的催化剂,在该反应中高活性是重要的。特别是当与加氢组分如铂、钯或铼相结合时,ZSM-12可用于C9+烷基芳族烃的单独或在甲苯和/或苯存在下的催化转化中以生产二甲苯。该转化典型地在温度约650-约950°F(340-510℃),优选约750-约850°F(400-450℃);压力约100-约600psig(790-4240kPa),优选约200-约500psig(1480-3550kPa);重时空速(WHSV)介于约0.1-约200hr-1,优选介于约0.5-约20hr-1下,和氢(H2)与烃(HC)的摩尔比率介于约1-约5,优选介于约1-约3下进行。
当本发明的ZSM-12用于C9+烷基芳族烃的催化转化时,ZSM-12可以与约束指数3-12的第二种分子筛相结合使用,例如ZSM-5、ZSM-11、ZSM-22、ZSM-23、ZSM-35、ZSM-48、ZSM-57和ZSM-58。ZSM-12与第二种分子筛可以在独立的催化床中排列,具有从含有ZSM-12的催化剂床到含有第二种分子筛的床的进料级联(feed cascading)。另外,ZSM-12与第二种分子筛能够在单个催化床中相结合。
为了更充分说明本发明的性质和实施本发明的方式,给出下列实施例。
实施例1(对比)
从306g水,83g 50%的溴化四乙基铵(TEABr),64.3g UltrasilPM,1.55g氢氧化铝和15.8g 50%氢氧化钠溶液制备混合物。该混合物有以下摩尔组成:
SiO2/Al2O3=100
H2O/SiO2=20
OH-/SiO2=0.2
Na+/SiO2=0.2
TEABr/SiO2=0.2
该混合物在600ml高压反应釜中在285°F(140℃)下以150RPM的搅拌速度反应168小时。产物进行过滤,用去离子水(DI)洗涤并在温度250°F(120℃)下干燥。所合成的材料的XRD图案显示为ZSM-12拓扑结构的典型纯相。所合成的材料的SEM照片示于图1中,并表明材料由小晶体的聚结物组成(平均晶体尺寸大约为0.05微米)。
所合成的晶体通过在室温下与硝酸铵溶液进行两次离子交换,然后在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时而转化成氢形式。所得到的ZSM-12晶体具有SiO2/Al2O3摩尔比为116,α值为120,和对于100℃的1,3,5-三甲基苯(均三甲基苯)的D/r2参数为7900×10-6。
实施例2(对比)
使用与实施例1同样的反应物和反应程序,只是将溴化甲基三乙基铵(MTEA)用作定向剂。
所合成的材料的SEM照片示于图2中,并表明材料由稻谷状晶体的聚结物组成(平均晶体尺寸1-5微米)。
所合成的晶体通过在室温下与硝酸铵溶液进行两次离子交换,然后在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时而转化成氢形式。所得到的ZSM-12晶体具有SiO2/Al2O3摩尔比为116,α值为92,和对于100℃的1,3,5-三甲基苯(均三甲基苯)的D/r2参数为19×10-6。
实施例3(对比)
从348g水,30g氯化甲基三乙基铵(MTEACl),64.3g UltrasilPM,2.33g氢氧化铝和17.4g50%氢氧化钠溶液制备混合物。该混合物有以下摩尔组成:
SiO2/Al2O3=67
H2O/SiO2=20
OH-/SiO2=0.22
Na+/SiO2=0.22
MTEACl/SiO2=0.2
该混合物在600ml高压反应釜中在285°F(140℃)下以150RPM的搅拌速度反应168小时。产物进行过滤,用去离子水(DI)洗涤并在温度250°F(120℃)下干燥。所合成的材料的XRD图案显示为ZSM-12拓扑结构的典型纯相。所合成材料的SEM示于图3中,并表明材料由小晶体的聚结物组成(平均晶体尺寸大约为0.05微米)。
所合成的晶体通过在室温下与硝酸铵溶液进行两次离子交换,然后在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时而转化成氢形式。所得到的ZSM-12晶体具有SiO2/Al2O3摩尔比为68.6,α值为190,和对于100℃的1,3,5-三甲基苯(均三甲基苯)的D/r2参数为600×10-6。
实施例4
从1158g水,85g氯化甲基三乙基铵(MTEACl),178g UltrasilPM,17g铝酸钠溶液(45%)和35g 50%氢氧化钠溶液制备混合物。该混合物有以下摩尔组成:
SiO2/Al2O3=60
H2O/SiO2=24.5
OH-/SiO2=0.2
Na+/SiO2=.2
MTEACl/SiO2=0.21
该混合物在2L高压反应釜中于320°F(160℃)下以150RPM的搅拌速度反应168小时。产物进行过滤,用去离子水(DI)洗涤并在温度250°F(120℃)下干燥。所合成材料的XRD图案显示为ZSM-12拓扑结构的典型纯相。所合成材料的SEM与图3示出的相似,表明材料由小晶体的聚结物组成(平均晶体尺寸大约为0.05微米)。
所合成的晶体通过在室温下与硝酸铵溶液进行两次离子交换,然后在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时而转化成氢形式。所得到的ZSM-12晶体具有SiO2/Al2O3摩尔比为58.1,α值为340,和对于100℃1,3,5-三甲基苯(均三甲基苯)的D/r2参数为1150×10-6。
实施例5
从1204g水,105g溴化甲基三乙基铵(MTEABr),283g硅酸钠溶液,16.8g硝酸铝和16.45硫酸(98%溶液)制备混合物。该混合物有以下摩尔组成:
SiO2/Al2O3=60
H2O/SiO2=57
OH-/SiO2=0.3
Na+/SiO2=0.6
MTEABr/SiO2=0.4
该混合物在2L高压反应釜中在320°F(160℃)下以150RPM的搅拌速度反应120小时。产物进行过滤,用去离子水(DI)洗涤并在温度250°F(120℃)下干燥。所合成材料的XRD图案显示为ZSM-12拓扑结构的典型纯相。所合成材料的SEM与图3示出的相似,表明材料由小晶体的聚结物组成(平均晶体尺寸大约为0.05微米)。
所合成的晶体通过在室温下与硝酸铵溶液进行两次离子交换,然后在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时而转化成氢形式。所得到的ZSM-12晶体具有SiO2/Al2O3摩尔比为51.8,α值为330,和对于100℃的1,3,5-三甲基苯(均三甲基苯)的D/r2参数为1400×10-6。
实施例6
从1185g水,98g氯化甲基三乙基铵(MTEACl),204.5g UltrasilPM,24g铝酸钠溶液(45%)和43.2g 50%氢氧化钠溶液制备混合物。该混合物有以下摩尔组成:
SiO2/Al2O3=50
H2O/SiO2=22
OH-/SiO2=0.22
Na+/SiO2=0.22
MTEACl/SiO2=0.2
该混合物在2L高压反应釜中在285°F(140℃)下以150RPM的搅拌速度反应336小时。产物进行过滤,用去离子水(DI)洗涤并在温度250°F(120℃)下干燥。所合成材料的XRD图案显示为ZSM-12拓扑结构的典型纯相。所合成材料的SEM与图3示出的相似,表明材料由小晶体的聚结物组成(平均晶体尺寸大约为0.05微米)。
所合成的晶体通过在室温下与硝酸铵溶液进行两次离子交换,然后在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时而转化成氢形式。所得到的ZSM-12晶体具有SiO2/Al2O3摩尔比为46.3,α值为472,和对于100℃的1,3,5-三甲基苯(均三甲基苯)的D/r2参数为3600×10-6。
实施例7
具有与实施例3中同样组成的反应混合物与0.5wt%的在实施例3得到的ZSM-12种晶相混合,并在5加仑高压反应釜中在320°F(160℃)下以150RPM的搅拌速度反应120小时。产物进行过滤,用去离子水(DI)洗涤并在温度120℃下干燥。所合成材料的XRD图案显示为ZSM-12拓扑结构的典型纯相。所合成材料的SEM示于图4中,并表明材料由小晶体的聚结物组成(平均晶体尺寸大约为0.05微米)。
所合成的晶体通过在室温下与硝酸铵溶液进行两次离子交换,然后在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时而转化成氢形式。所得到的ZSM-12晶体具有SiO2/Al2O3摩尔比为48.2,α值为560,和对于100℃的1,3,5-三甲基苯(均三甲基苯)的D/r2参数为8450×10-6。
在图5中绘制了实施例1-7的ZSM-12晶体的相对活性和SiO2/Al2O3组成。可以从图5看出,具有SiO2/Al2O3<60以及呈现小晶体的聚结物形式的所需形态的ZSM-12晶体能够通过使用MTEA氢氧化物或它们的盐在260-320°F(140-160℃)下在搅拌条件下生产。
实施例8
ZSM-12/氧化铝催化剂是从与35份LaRoche Versal 300氧化铝混合的65份的在实施例5生产的氢形式的ZSM-12晶体制备的(按干基计算)。该混合物研糊形成为1/16″圆筒形挤出物。得到的挤出物在250°F(120℃)下干燥并在1000°F(540℃)下煅烧6小时。最终得到的挤出物具有α值为316。
最终得到的挤出物然后经由初始润湿浸渍法用高铼酸铵(APR)溶液浸渍,在挤出物上获得0.5wt%Re。挤出物在250°F(120℃)下干燥2小时,然后在空气中于975°F(524℃)下煅烧1小时。该浸渍和煅烧后的挤出物在100%蒸气中于900°F(482℃)下蒸5.5小时。最终的催化剂包含0.44wt%Re和具有α值为60。
实施例9
在实施例8得到的催化剂在含有大约60wt%甲苯并具有下表2给出的精确组成的C9+芳族进料的催化转化中进行试验。催化作用评价是在具有3/8”(9.5mm)外直径的反应管的微型装置中进行,将催化剂装入反应管中,并与作为填充材料的砂子混合。在装入反应器中后,催化剂在200℃下干燥2小时,并在427℃和340psig(2445kPa)的氢压下用氢气还原1小时。反应器然后在氮气下加热到反应温度427℃,反应在340psig(2445kPa)的压力下进行,氢与烃的摩尔比率为1.2和WHSV为3-6。结果列于下表2中。
表2
WHSV | 6.00 | 3.00 | 3.00 | 3.00 | 3.00 | 3.00 | 3.00 | |
运转天数 | 1.13 | 1.90 | 2.83 | 3.83 | 4.83 | 5.42 | 6.42 | |
产率,wt% | 进料 | 产物 | ||||||
甲烷 | 1.27 | 1.06 | 1.27 | 0.33 | 0.08 | 0.08 | 0.08 | |
C2 | 2.09 | 2.22 | 2.09 | 2.16 | 2.09 | 2.09 | 2.09 | |
丙烯 | 1.16 | 1.19 | 1.16 | 1.46 | 1.51 | 1.51 | 1.51 | |
C4 | 0.70 | 0.55 | 0.68 | 0.68 | 0.74 | 0.64 | 0.70 | |
C5 | 0.11 | 0.08 | 0.11 | 0.07 | 0.08 | 0.08 | 0.08 | |
C6非A | 0.36 | 0.36 | 0.27 | 0.27 | 0.27 | 0.27 | 0.30 | |
C7非A | 0.02 | 0.01 | 0.02 | 0.01 | 0.01 | 0.01 | 0.01 | |
苯 | 9.43 | 9.58 | 11.19 | 11.35 | 11.60 | 11.47 | 11.76 | |
甲苯 | 62.95 | 39.87 | 39.97 | 36.60 | 36.37 | 36.72 | 36.52 | 37.84 |
乙基苯 | 0.05 | 1.59 | 1.65 | 1.11 | 1.06 | 1.12 | 1.09 | 1.31 |
二甲苯 | 3.26 | 26.98 | 26.80 | 31.09 | 31.54 | 31.30 | 31.53 | 29.46 |
异丙基苯 | 0.34 | 0.01 | 0.01 | 0.01 | 0.01 | 0.00 | 0.01 | 0.01 |
n-丙基苯 | 1.05 | 0.01 | 0.01 | 0.01 | 0.01 | 0.01 | 0.01 | 0.01 |
乙基甲苯 | 12.72 | 3.53 | 3.68 | 1.79 | 1.77 | 1.77 | 1.80 | 2.28 |
三甲基苯 | 18.58 | 10.16 | 10.05 | 9.64 | 9.91 | 9.70 | 9.85 | 9.54 |
二乙基苯 | 0.37 | 0.06 | 0.07 | 0.03 | 0.03 | 0.03 | 0.03 | 0.04 |
二甲基乙基苯 | 0.44 | 0.74 | 0.77 | 0.54 | 0.55 | 0.55 | 0.56 | 0.63 |
四甲基苯 | 0.00 | 0.50 | 0.49 | 0.64 | 0.67 | 0.65 | 0.66 | 0.58 |
茚满 | 0.21 | 0.33 | 0.34 | 0.25 | 0.26 | 0.25 | 0.26 | 0.28 |
甲基茚满 | 0.08 | 0.08 | 0.10 | 0.11 | 0.10 | 0.10 | 0.09 | |
萘 | 0.08 | 0.08 | 0.08 | 0.08 | 0.08 | 0.08 | 0.08 | |
甲基萘 | 0.22 | 0.22 | 0.35 | 0.37 | 0.35 | 0.36 | 0.34 | |
其它 | 0.05 | 0.70 | 0.72 | 0.96 | 0.93 | 0.99 | 1.02 | 1.01 |
甲苯转化率(wt%) | 36.66 | 36.50 | 41.87 | 42.22 | 41.66 | 41.98 | 39.90 | |
A9+转化率(wt%) | 51.59 | 51.26 | 57.83 | 56.80 | 57.40 | 56.77 | 56.30 | |
甲苯加A9+转化率(wt%) | 41.88 | 41.61 | 47.47 | 47.20 | 47.02 | 47.03 | 45.48 | |
BTX(wt%) | 66.21 | 76.28 | 76.35 | 78.88 | 79.27 | 79.63 | 79.52 | 79.05 |
苯纯度(%C6) | 96.36 | 96.39 | 97.61 | 97.67 | 97.73 | 97.67 | 97.52 | |
环损耗(mol%) | 4.02 | 3.76 | 3.73 | 3.09 | 2.80 | 2.82 | 2.64 | |
氢耗(%) | 13.42 | 11.23 | 10.77 | 4.39 | 1.98 | 1.73 | 1.43 |
实施例10
重复实施例10的过程,只是催化剂在与实施例10中所用的相同进料接触之前在900°F(482℃)下汽蒸了5.5小时。工艺条件与实施例10中相同且结果列于下表3。
表3
WHSV | 6 | 6 | 6 | 3 | 3 |
运转天数 | 1.13 | 1.90 | 2.83 | 3.83 | 4.83 |
产率,wt% | |||||
甲烷 | 1.27 | 1.06 | 1.27 | 0.33 | 0.08 |
C2 | 2.09 | 2.21 | 2.09 | 2.15 | 2.09 |
丙烯 | 1.16 | 1.19 | 1.16 | 1.45 | 1.51 |
C4 | 0.81 | 0.78 | 0.75 | 0.92 | 0.78 |
C5 | 0.11 | 0.08 | 0.11 | 0.07 | 0.08 |
C6非A | 0.37 | 0.37 | 0.37 | 0.34 | 0.32 |
C7非A | 0.02 | 0.01 | 0.02 | 0.01 | 0.01 |
苯 | 10.39 | 10.27 | 10.29 | 11.23 | 11.60 |
甲苯 | 36.92 | 36.65 | 37.33 | 40.86 | 36.67 |
乙基苯 | 1.73 | 1.74 | 1.79 | 1.40 | 1.37 |
二甲苯 | 29.12 | 29.28 | 28.65 | 26.23 | 30.25 |
n-丙基苯 | 0.01 | 0.01 | 0.01 | 0.00 | 0.01 |
乙基甲苯 | 3.38 | 3.43 | 3.51 | 1.04 | 2.43 |
三甲基苯 | 9.96 | 10.13 | 9.98 | 10.84 | 9.98 |
丙基甲苯 | 0.00 | 0.00 | 0.00 | 0.04 | 0.00 |
二乙基苯 | 0.07 | 0.07 | 0.07 | 0.01 | 0.04 |
二甲基乙基苯 | 0.77 | 0.78 | 0.77 | 0.70 | 0.65 |
四甲基苯 | 0.51 | 0.52 | 0.49 | 0.65 | 0.58 |
茚满 | 0.34 | 0.35 | 0.35 | 0.33 | 0.31 |
甲基茚满 | 0.08 | 0.08 | 0.08 | 0.10 | 0.09 |
萘 | 0.09 | 0.09 | 0.09 | 0.10 | 0.09 |
甲基萘 | 0.18 | 0.19 | 0.18 | 0.27 | 0.25 |
其它 | 0.63 | 0.69 | 0.64 | 0.93 | 0.82 |
甲苯转化率(wt%) | 41.35 | 41.77 | 40.69 | 35.09 | 41.74 |
A9+转化率(wt%) | 52.77 | 51.63 | 52.35 | 55.91 | 55.06 |
甲苯加A9+转化率(wt%) | 45.31 | 45.11 | 44.75 | 42.14 | 46.23 |
BTX(wt%) | 76.43 | 76.20 | 76.27 | 78.32 | 78.51 |
苯纯度(%C6) | 96.59 | 96.55 | 96.50 | 97.05 | 97.30 |
环损耗(mol%) | 4.15 | 4.20 | 4.10 | 2.87 | 2.89 |
氢耗(%) | 14.40 | 12.93 | 14.08 | 4.17 | 3.46 |
Claims (15)
1.一种具有ZSM-12骨架结构和符合以下摩尔关系式的组成的多孔结晶材料:
X2O3:(n)YO2
其中X是三价元素,Y是四价元素,n小于60,该材料的平均晶体尺寸小于0.1微米,和该材料在100℃的温度和2乇的均三甲苯压力下测量时对于均三甲苯的扩散参数至少为1000×10-6秒-1。
2.根据权利要求1的多孔结晶材料,其中n是20到小于60。
3.根据权利要求1或2的多孔结晶材料,其中X是铝,Y是硅。
4.根据前述权利要求任意一项的多孔结晶材料,其中所述材料具有大于150的α值。
5.根据前述权利要求任意一项的多孔结晶材料,其中所述材料具有大于300的α值。
6.合成权利要求1的多孔结晶材料的方法,包括以下步骤:
(a)制备能形成所述材料的混合物,所述混合物包含碱金属或碱土金属(M)源、三价元素(X)的氧化物、四价元素(Y)的氧化物、氢氧根离子(OH-)、水和甲基三乙基铵阳离子(R),其中所述混合物具有以下摩尔比率范围内的组成:
YO2/X2O3<100
H2O/YO2=10-100
OH-/YO2=0.1-0.6
M/YO2=0.1-0.6
R/YO2=0.1-0.6,
(b)保持所述混合物在足够的条件下,直到形成所述材料的晶体为止;和
(c)从步骤(ii)回收所述晶体材料。
7.根据权利要求6的方法,其中所述反应混合物具有以下摩尔比率范围内的组成:
YO2/X2O3=40-80
H2O/YO2=15-40
OH-/YO2=0.15-0.4
M/YO2=0.15-0.4
R/YO2=0.15-0.4。
8.根据权利要求6或7的方法,其中所述条件包括温度为170℃或170℃以下。
9.根据权利要求8的方法,其中所述条件包括温度为140-160℃。
10.根据权利要求6、7、8或9的方法,其中M是钠。
11.将C9+烷基芳香烃转化为包括二甲苯的产品的方法,包括在转化条件下使含有C9+烷基芳香烃和甲苯和/或苯的进料与根据权利要求1-5任意一项的多孔结晶材料或根据权利要求6-10任意一项方法制得的多孔结晶材料进行接触的步骤。
12.根据权利要求11的方法,其中转化条件包括:温度约650-950°F(340-510℃),压力约100-600psig(790-4240kPa),重时空速度介于约0.1-200hr-1,和氢与烃的摩尔比率介于约1-5。
13.根据权利要求11的方法,其中转化条件包括:温度约750-850°F(400-450℃),压力约200-500psig(1480-3550kPa),重时空速介于约0.5-20hr-1,和氢与烃的摩尔比率介于约1-3。
14.根据权利要求11、12或13的方法,其中所述进料还与约束指数3-12的第二种分子筛进行接触。
15.根据权利要求14的方法,其中所述第二种分子筛选自ZSM-5、ZSM-11、ZSM-22、ZSM-23、ZSM-35、ZSM-48、ZSM-57和ZSM-58。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/294,780 US6893624B2 (en) | 2002-11-15 | 2002-11-15 | High activity small crystal ZSM-12 |
US10/294,780 | 2002-11-15 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1774398A true CN1774398A (zh) | 2006-05-17 |
CN100404419C CN100404419C (zh) | 2008-07-23 |
Family
ID=32297040
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2003801051636A Expired - Fee Related CN100404419C (zh) | 2002-11-15 | 2003-10-17 | 高活性小晶体zsm-12 |
Country Status (9)
Country | Link |
---|---|
US (1) | US6893624B2 (zh) |
EP (1) | EP1560793A1 (zh) |
JP (1) | JP2006506311A (zh) |
KR (1) | KR101064796B1 (zh) |
CN (1) | CN100404419C (zh) |
AU (1) | AU2003284254A1 (zh) |
MY (1) | MY134623A (zh) |
TW (1) | TWI365104B (zh) |
WO (1) | WO2004046034A1 (zh) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101792153A (zh) * | 2010-03-02 | 2010-08-04 | 黑龙江大学 | 硅镓酸盐分子筛Ga-ZSM-12的合成方法 |
CN102574694A (zh) * | 2009-11-20 | 2012-07-11 | 雪佛龙美国公司 | 制备铝硅酸盐zsm-12的方法 |
CN103922362A (zh) * | 2014-04-19 | 2014-07-16 | 复旦大学 | 一种的mtw沸石及其制备方法 |
CN104785288A (zh) * | 2010-04-21 | 2015-07-22 | 埃克森美孚化学专利公司 | 二甲苯异构化方法及其催化剂 |
CN106564909A (zh) * | 2015-10-09 | 2017-04-19 | 中国石油化工股份有限公司 | 一种zsm-12分子筛的制备方法 |
CN107418618A (zh) * | 2016-04-26 | 2017-12-01 | Sk新技术株式会社 | 降低重质基础油中的浊度的方法以及具有降低的浊度的加氢异构化催化系统 |
CN108290749A (zh) * | 2015-12-04 | 2018-07-17 | 埃克森美孚研究工程公司 | Emm-28新型合成结晶材料、其制备和用途 |
Families Citing this family (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7553791B2 (en) | 2002-11-14 | 2009-06-30 | Exxonmobil Chemical Patents Inc. | Heavy aromatics conversion catalyst composition and processes therefor and therewith |
DE10314753A1 (de) * | 2003-04-01 | 2004-10-14 | Süd-Chemie AG | Synthetischer Zeolith, insbesondere für die katalytische Hydroisomerisierung von höheren Paraffinen |
EP1922390A2 (en) * | 2005-08-04 | 2008-05-21 | Chevron U.S.A., Inc. | Dewaxing process using zeolites mtt and mtw |
US8816145B2 (en) | 2007-06-21 | 2014-08-26 | Exxonmobil Chemical Patents Inc. | Liquid phase alkylation process |
US20090093662A1 (en) * | 2007-10-08 | 2009-04-09 | Whitchurch Patrick C | Aromatic isomerization catalyst |
US8030240B2 (en) * | 2007-12-28 | 2011-10-04 | Exxonmobil Research And Engineering Company | Multiple molecular sieve catalyst for sour service dewaxing |
US7626064B1 (en) * | 2008-06-26 | 2009-12-01 | Uop Llc | Transalkylation process |
WO2010000652A1 (en) | 2008-07-04 | 2010-01-07 | Shell Internationale Research Maatschappij B.V. | Catalyst and isomerisation process |
US20110034749A1 (en) * | 2009-08-07 | 2011-02-10 | Exxonmobil Research And Engineering Company | Synthesis and use of ZSM-12 |
US8202506B2 (en) | 2009-11-17 | 2012-06-19 | Exxonmobil Research And Engineering Company | High activity small crystal ZSM-12 |
US8101811B2 (en) * | 2009-11-20 | 2012-01-24 | Chevron U.S.A. Inc. | Process for isomerizing a hydrocarbonaceous feedstock using aluminosilicate ZSM-12 |
EP2455161A1 (en) | 2010-11-18 | 2012-05-23 | Shell Internationale Research Maatschappij B.V. | Isomerisation catalyst preparation process |
EP2455160A1 (en) | 2010-11-18 | 2012-05-23 | Shell Internationale Research Maatschappij B.V. | Isomerisation catalyst preparation process |
TWI483775B (zh) * | 2011-09-16 | 2015-05-11 | Exxonmobil Chem Patents Inc | 經改善之mcm-56製法 |
WO2013090534A1 (en) | 2011-12-16 | 2013-06-20 | Shell Oil Company | A titania-bound zsm-12 zeolite composition and method of making and using such composition |
KR101950552B1 (ko) | 2012-12-07 | 2019-02-20 | 엑손모빌 리서치 앤드 엔지니어링 컴퍼니 | 개선된 모폴로지를 갖는 zsm-5 결정의 합성 |
US9522858B2 (en) | 2013-05-31 | 2016-12-20 | Exxonmobil Chemical Patents Inc. | Transalkylation system |
US10450243B2 (en) | 2014-12-19 | 2019-10-22 | Exxonmobil Chemical Patents Inc. | Sulfiding process for aromatic transalkylations |
DK3554693T3 (da) | 2016-12-16 | 2022-10-24 | Shell Int Research | Katalysatorsystem til afvoksning |
EP3724156B1 (en) | 2017-12-14 | 2023-05-10 | ExxonMobil Chemical Patents Inc. | Processes for isomerizing alpha olefins |
WO2019201627A1 (en) | 2018-04-17 | 2019-10-24 | Shell Internationale Research Maatschappij B.V. | Catalyst system for dewaxing |
CN112939009B (zh) * | 2019-12-11 | 2022-11-15 | 中国科学院大连化学物理研究所 | 一种mtw型分子筛的固相合成方法 |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3832449A (en) | 1971-03-18 | 1974-08-27 | Mobil Oil Corp | Crystalline zeolite zsm{14 12 |
US4537758A (en) | 1979-03-21 | 1985-08-27 | Mobil Oil Corporation | Process for preparing highly siliceous porous ZSM-12 type crystalline material |
US4452769A (en) | 1979-03-21 | 1984-06-05 | Mobil Oil Corporation | Method of preparing crystalline zeolite |
US4391785A (en) | 1981-12-21 | 1983-07-05 | Mobil Oil Corporation | Preparation of ZSM-12 type zeolites |
US4665268A (en) * | 1982-09-30 | 1987-05-12 | Mobil Oil Corporation | Catalytic conversion of methanol to light olefins |
US4552739A (en) | 1983-12-09 | 1985-11-12 | Mobil Oil Corporation | Method of preparing crystalline zeolite ZSM-12 and product |
US4539193A (en) | 1984-05-23 | 1985-09-03 | Mobil Oil Corporation | Synthesis of crystalline silicate ZSM-12 |
US4552738A (en) | 1984-05-25 | 1985-11-12 | Mobil Oil Corporation | Synthesis of crystalline silicate ZSM-12 |
CA1239385A (en) | 1984-06-26 | 1988-07-19 | Mae K. Rubin | Preparation of zeolite zsm-12 |
US4585637A (en) | 1984-06-26 | 1986-04-29 | Mobil Oil Corporation | Synthesis of crystalline silicate ZSM-12 |
US4585746A (en) | 1984-06-27 | 1986-04-29 | Mobil Oil Corporation | Synthesis of crystalline silicate ZSM-12 |
US5021141A (en) | 1990-09-14 | 1991-06-04 | Mobil Oil Corp. | Synthesis of crystalline ZSM-12 type structure |
FR2670772B1 (fr) * | 1990-12-21 | 1993-04-09 | Inst Francais Du Petrole | Zeolithe de type mtw et son procede de preparation. |
US5192521A (en) | 1991-11-19 | 1993-03-09 | Mobil Oil Corp. | Synthesis of crystalline silicate ZSM-12 |
US5905051A (en) | 1997-06-04 | 1999-05-18 | Wu; An-Hsiang | Hydrotreating catalyst composition and processes therefor and therewith |
US5942651A (en) | 1997-06-13 | 1999-08-24 | Mobile Oil Corporation | Process for converting C9 + aromatic hydrocarbons to lighter aromatic products by transalkylation in the prescence of two zeolite-containing catalysts |
JPH11100381A (ja) * | 1997-09-29 | 1999-04-13 | Showa Denko Kk | ジアザスピロノナニウム塩 |
US6652832B2 (en) * | 2001-02-05 | 2003-11-25 | Exxonmobil Oil Corporation | Synthesis of ZSM-12 |
US7308067B2 (en) * | 2003-08-04 | 2007-12-11 | Intel Corporation | Read bias scheme for phase change memories |
-
2002
- 2002-11-15 US US10/294,780 patent/US6893624B2/en not_active Expired - Lifetime
-
2003
- 2003-10-13 TW TW092128316A patent/TWI365104B/zh not_active IP Right Cessation
- 2003-10-17 AU AU2003284254A patent/AU2003284254A1/en not_active Abandoned
- 2003-10-17 EP EP03776434A patent/EP1560793A1/en not_active Withdrawn
- 2003-10-17 CN CNB2003801051636A patent/CN100404419C/zh not_active Expired - Fee Related
- 2003-10-17 JP JP2004553449A patent/JP2006506311A/ja active Pending
- 2003-10-17 WO PCT/US2003/032853 patent/WO2004046034A1/en active Application Filing
- 2003-10-17 KR KR1020057008781A patent/KR101064796B1/ko not_active IP Right Cessation
- 2003-10-21 MY MYPI20034012A patent/MY134623A/en unknown
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102574694A (zh) * | 2009-11-20 | 2012-07-11 | 雪佛龙美国公司 | 制备铝硅酸盐zsm-12的方法 |
CN101792153A (zh) * | 2010-03-02 | 2010-08-04 | 黑龙江大学 | 硅镓酸盐分子筛Ga-ZSM-12的合成方法 |
CN101792153B (zh) * | 2010-03-02 | 2012-03-07 | 黑龙江大学 | 硅镓酸盐分子筛Ga-ZSM-12的合成方法 |
CN104785288A (zh) * | 2010-04-21 | 2015-07-22 | 埃克森美孚化学专利公司 | 二甲苯异构化方法及其催化剂 |
CN103922362A (zh) * | 2014-04-19 | 2014-07-16 | 复旦大学 | 一种的mtw沸石及其制备方法 |
CN106564909A (zh) * | 2015-10-09 | 2017-04-19 | 中国石油化工股份有限公司 | 一种zsm-12分子筛的制备方法 |
CN106564909B (zh) * | 2015-10-09 | 2018-11-30 | 中国石油化工股份有限公司 | 一种zsm-12分子筛的制备方法 |
CN108290749A (zh) * | 2015-12-04 | 2018-07-17 | 埃克森美孚研究工程公司 | Emm-28新型合成结晶材料、其制备和用途 |
CN108290749B (zh) * | 2015-12-04 | 2022-06-24 | 埃克森美孚科技工程公司 | Emm-28新型合成结晶材料、其制备和用途 |
CN107418618A (zh) * | 2016-04-26 | 2017-12-01 | Sk新技术株式会社 | 降低重质基础油中的浊度的方法以及具有降低的浊度的加氢异构化催化系统 |
CN107418618B (zh) * | 2016-04-26 | 2021-07-09 | Sk新技术株式会社 | 降低重质基础油中的浊度的方法以及具有降低的浊度的加氢异构化催化系统 |
Also Published As
Publication number | Publication date |
---|---|
WO2004046034A1 (en) | 2004-06-03 |
US20040097363A1 (en) | 2004-05-20 |
AU2003284254A1 (en) | 2004-06-15 |
KR20050085004A (ko) | 2005-08-29 |
US6893624B2 (en) | 2005-05-17 |
CN100404419C (zh) | 2008-07-23 |
KR101064796B1 (ko) | 2011-09-14 |
JP2006506311A (ja) | 2006-02-23 |
TWI365104B (en) | 2012-06-01 |
EP1560793A1 (en) | 2005-08-10 |
TW200420350A (en) | 2004-10-16 |
MY134623A (en) | 2007-12-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1774398A (zh) | 高活性小晶体zsm-12 | |
CN102066529B (zh) | 烷基转移方法 | |
CN1512964A (zh) | 合成的多孔晶体材料itq-12、其合成及应用 | |
CN1291914C (zh) | 合成的多孔晶体材料itq-13、其合成及应用 | |
CA2779371C (en) | High activity small crystal zsm-12 | |
CN1367758A (zh) | Zsm-5和zsm-11的合成方法 | |
JP5852749B2 (ja) | Uzm−39アルミノシリケートゼオライトを用いた芳香族化合物の転化反応 | |
JP2017501960A (ja) | Zsm−48結晶の合成 | |
CN104812703A (zh) | 具有改进形态的zsm-5晶体的合成 | |
CN106587102B (zh) | Zsm-12型沸石分子筛的合成方法 | |
WO2011017506A2 (en) | Synthesis and use of zsm-12 | |
JP5816512B2 (ja) | 大きな細孔容積を有するnu−85分子篩およびその製造方法 | |
JP5990594B2 (ja) | 高活性大結晶zsm−5の合成 | |
JP2024511577A (ja) | 小さな結晶ssz-41、その合成及び使用 | |
WO2015021611A1 (zh) | 一种ZSM-22分子筛及Me-ZSM-22的合成方法 | |
CN111712462B (zh) | Emm-37材料及其方法和用途 | |
CN1016678B (zh) | 结晶硅酸盐zsm-11之合成 | |
CN1487904A (zh) | 结晶状分子筛组合物mcm-65、其合成和应用 | |
CN1276875C (zh) | 一种分子筛的合成方法 | |
CN1166751C (zh) | 形状选择性沸石催化剂及其在芳族化合物转化中的应用 | |
CN1197770C (zh) | 合成的多孔结晶状mcm-71、其合成方法和应用 | |
CA2872869C (en) | Zeolite zsm-18, its synthesis and its use | |
CN113683098A (zh) | 一种动态合成GaKL分子筛的方法及应用 | |
CN107952470A (zh) | 复合分子筛的合成方法及应用 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080723 Termination date: 20171017 |
|
CF01 | Termination of patent right due to non-payment of annual fee |