RU2005121263A - Мезопористые материалы с активными металлами - Google Patents
Мезопористые материалы с активными металлами Download PDFInfo
- Publication number
- RU2005121263A RU2005121263A RU2005121263/04A RU2005121263A RU2005121263A RU 2005121263 A RU2005121263 A RU 2005121263A RU 2005121263/04 A RU2005121263/04 A RU 2005121263/04A RU 2005121263 A RU2005121263 A RU 2005121263A RU 2005121263 A RU2005121263 A RU 2005121263A
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- RU
- Russia
- Prior art keywords
- group
- heteroatom
- feedstock
- combinations
- processing method
- Prior art date
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- 229910052751 metal Inorganic materials 0.000 title claims 2
- 239000002184 metal Substances 0.000 title claims 2
- 150000002739 metals Chemical class 0.000 title claims 2
- 239000013335 mesoporous material Substances 0.000 title 1
- 238000000034 method Methods 0.000 claims 41
- 125000005842 heteroatom Chemical group 0.000 claims 18
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims 12
- 229910052742 iron Inorganic materials 0.000 claims 11
- 238000003672 processing method Methods 0.000 claims 11
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 8
- 229910052782 aluminium Inorganic materials 0.000 claims 7
- 229910052804 chromium Inorganic materials 0.000 claims 7
- 239000011651 chromium Substances 0.000 claims 7
- 229910052759 nickel Inorganic materials 0.000 claims 7
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims 6
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims 6
- 239000010949 copper Substances 0.000 claims 6
- QXYJCZRRLLQGCR-UHFFFAOYSA-N dioxomolybdenum Chemical compound O=[Mo]=O QXYJCZRRLLQGCR-UHFFFAOYSA-N 0.000 claims 6
- 229910052733 gallium Inorganic materials 0.000 claims 6
- 239000011148 porous material Substances 0.000 claims 6
- 229910052719 titanium Inorganic materials 0.000 claims 6
- 239000010936 titanium Substances 0.000 claims 6
- 229910052720 vanadium Inorganic materials 0.000 claims 6
- 150000001491 aromatic compounds Chemical class 0.000 claims 5
- 229910052802 copper Inorganic materials 0.000 claims 5
- 239000000463 material Substances 0.000 claims 5
- 229910052763 palladium Inorganic materials 0.000 claims 5
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 claims 4
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 claims 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 4
- 239000003054 catalyst Substances 0.000 claims 4
- 230000003197 catalytic effect Effects 0.000 claims 4
- 238000005336 cracking Methods 0.000 claims 4
- 238000007324 demetalation reaction Methods 0.000 claims 4
- 229910052750 molybdenum Inorganic materials 0.000 claims 4
- 230000003647 oxidation Effects 0.000 claims 4
- 238000007254 oxidation reaction Methods 0.000 claims 4
- 239000000377 silicon dioxide Substances 0.000 claims 4
- 229910052718 tin Inorganic materials 0.000 claims 4
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 claims 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims 3
- 150000001336 alkenes Chemical group 0.000 claims 3
- 229940100198 alkylating agent Drugs 0.000 claims 3
- 239000002168 alkylating agent Substances 0.000 claims 3
- 125000004429 atom Chemical group 0.000 claims 3
- 229910052738 indium Inorganic materials 0.000 claims 3
- 229910052748 manganese Inorganic materials 0.000 claims 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims 3
- 150000002894 organic compounds Chemical class 0.000 claims 3
- 229910052697 platinum Inorganic materials 0.000 claims 3
- 239000004408 titanium dioxide Substances 0.000 claims 3
- 229910052721 tungsten Inorganic materials 0.000 claims 3
- 229910052725 zinc Inorganic materials 0.000 claims 3
- 239000011701 zinc Substances 0.000 claims 3
- 229910052726 zirconium Inorganic materials 0.000 claims 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims 2
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 claims 2
- GQEZCXVZFLOKMC-UHFFFAOYSA-N 1-hexadecene Chemical compound CCCCCCCCCCCCCCC=C GQEZCXVZFLOKMC-UHFFFAOYSA-N 0.000 claims 2
- ICKWICRCANNIBI-UHFFFAOYSA-N 2,4-di-tert-butylphenol Chemical compound CC(C)(C)C1=CC=C(O)C(C(C)(C)C)=C1 ICKWICRCANNIBI-UHFFFAOYSA-N 0.000 claims 2
- KWOLFJPFCHCOCG-UHFFFAOYSA-N Acetophenone Chemical compound CC(=O)C1=CC=CC=C1 KWOLFJPFCHCOCG-UHFFFAOYSA-N 0.000 claims 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims 2
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 claims 2
- 238000002441 X-ray diffraction Methods 0.000 claims 2
- 230000010933 acylation Effects 0.000 claims 2
- 238000005917 acylation reaction Methods 0.000 claims 2
- 230000029936 alkylation Effects 0.000 claims 2
- 238000005804 alkylation reaction Methods 0.000 claims 2
- 229910000423 chromium oxide Inorganic materials 0.000 claims 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 claims 2
- 238000006356 dehydrogenation reaction Methods 0.000 claims 2
- 238000006477 desulfuration reaction Methods 0.000 claims 2
- 230000023556 desulfurization Effects 0.000 claims 2
- QDOXWKRWXJOMAK-UHFFFAOYSA-N dichromium trioxide Chemical compound O=[Cr]O[Cr]=O QDOXWKRWXJOMAK-UHFFFAOYSA-N 0.000 claims 2
- 150000004820 halides Chemical class 0.000 claims 2
- 229930195733 hydrocarbon Natural products 0.000 claims 2
- 150000002430 hydrocarbons Chemical class 0.000 claims 2
- 230000033444 hydroxylation Effects 0.000 claims 2
- 238000005805 hydroxylation reaction Methods 0.000 claims 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 claims 2
- 238000006317 isomerization reaction Methods 0.000 claims 2
- 229910052749 magnesium Inorganic materials 0.000 claims 2
- 239000003921 oil Substances 0.000 claims 2
- 238000006384 oligomerization reaction Methods 0.000 claims 2
- YNPNZTXNASCQKK-UHFFFAOYSA-N phenanthrene Chemical compound C1=CC=C2C3=CC=CC=C3C=CC2=C1 YNPNZTXNASCQKK-UHFFFAOYSA-N 0.000 claims 2
- 238000011084 recovery Methods 0.000 claims 2
- 235000012239 silicon dioxide Nutrition 0.000 claims 2
- 239000011135 tin Substances 0.000 claims 2
- 239000008096 xylene Substances 0.000 claims 2
- KJCVRFUGPWSIIH-UHFFFAOYSA-N 1-naphthol Chemical compound C1=CC=C2C(O)=CC=CC2=C1 KJCVRFUGPWSIIH-UHFFFAOYSA-N 0.000 claims 1
- PMPBFICDXLLSRM-UHFFFAOYSA-N 1-propan-2-ylnaphthalene Chemical compound C1=CC=C2C(C(C)C)=CC=CC2=C1 PMPBFICDXLLSRM-UHFFFAOYSA-N 0.000 claims 1
- LUZDYPLAQQGJEA-UHFFFAOYSA-N 2-Methoxynaphthalene Chemical compound C1=CC=CC2=CC(OC)=CC=C21 LUZDYPLAQQGJEA-UHFFFAOYSA-N 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 239000004215 Carbon black (E152) Substances 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- -1 Co Inorganic materials 0.000 claims 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims 1
- 239000005977 Ethylene Substances 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims 1
- 229910021536 Zeolite Inorganic materials 0.000 claims 1
- 150000001335 aliphatic alkanes Chemical class 0.000 claims 1
- 229910052785 arsenic Inorganic materials 0.000 claims 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims 1
- 239000011230 binding agent Substances 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 229910002091 carbon monoxide Inorganic materials 0.000 claims 1
- 238000004523 catalytic cracking Methods 0.000 claims 1
- 238000004517 catalytic hydrocracking Methods 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- MVPPADPHJFYWMZ-IDEBNGHGSA-N chlorobenzene Chemical group Cl[13C]1=[13CH][13CH]=[13CH][13CH]=[13CH]1 MVPPADPHJFYWMZ-IDEBNGHGSA-N 0.000 claims 1
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Substances ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 claims 1
- 239000004927 clay Substances 0.000 claims 1
- 229910052570 clay Inorganic materials 0.000 claims 1
- 239000003245 coal Substances 0.000 claims 1
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 claims 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims 1
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 238000005984 hydrogenation reaction Methods 0.000 claims 1
- 239000001282 iso-butane Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims 1
- 239000004058 oil shale Substances 0.000 claims 1
- 239000007800 oxidant agent Substances 0.000 claims 1
- 239000010690 paraffinic oil Substances 0.000 claims 1
- 239000001294 propane Substances 0.000 claims 1
- 229910052707 ruthenium Inorganic materials 0.000 claims 1
- 229930195734 saturated hydrocarbon Natural products 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 claims 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims 1
- 239000010457 zeolite Substances 0.000 claims 1
Classifications
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- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
- C10G2/33—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used
- C10G2/331—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals
- C10G2/332—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals of the iron-group
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- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/08—Silica
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- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/12—Silica and alumina
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- 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
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/26—Chromium
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- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
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- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/44—Palladium
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- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/50—Silver
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- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/52—Gold
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- 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
- B01J29/005—Mixtures of molecular sieves comprising at least one molecular sieve which is not an aluminosilicate zeolite, e.g. from groups B01J29/03 - B01J29/049 or B01J29/82 - B01J29/89
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- 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
- B01J29/03—Catalysts comprising molecular sieves not having base-exchange properties
- B01J29/0308—Mesoporous materials not having base exchange properties, e.g. Si-MCM-41
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J29/041—Mesoporous materials having base exchange properties, e.g. Si/Al-MCM-41
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/041—Mesoporous materials having base exchange properties, e.g. Si/Al-MCM-41
- B01J29/042—Mesoporous materials having base exchange properties, e.g. Si/Al-MCM-41 containing iron group metals, noble metals or copper
- B01J29/044—Iron group metals or copper
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- 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
- B01J29/041—Mesoporous materials having base exchange properties, e.g. Si/Al-MCM-41
- B01J29/045—Mesoporous materials having base exchange properties, e.g. Si/Al-MCM-41 containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
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- 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
- B01J29/046—Chromiasilicates; Aluminochromosilicates
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- 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
- B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
- B01J29/084—Y-type faujasite
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- 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
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
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- 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
- B01J29/7007—Zeolite Beta
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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Claims (36)
1. Способ обработки органических соединений, который содержит
а) обеспечение композиции, которая включает в себя, по существу, мезопористую структуру, образованную одним или несколькими материалами, выбранными из группы, состоящей из диоксида кремния, оксида алюминия, диоксида титана, оксида хрома, оксида железа, диоксида молибдена, причем указанная мезопористая структура содержит, по меньшей мере, 97 об.% пор, имеющих размер пор в интервале от примерно 15 до примерно 300 Е, и имеет объем микропор, по меньшей мере, примерно 0,01 см3/г, и где мезопористая структура имеет введенный в нее в количестве, по меньшей мере, примерно 0,02 мас.%, по меньшей мере, один каталитически и/или химически активный гетероатом, выбранный из группы, состоящей из Al, Ti, V, Cr, Zn, Fe, Sn, Mo, Ga, Ni, Co, In, Zr, Mn, Cu, Mg, Pd, Ru, W и их комбинаций, причем упомянутый катализатор имеет рентгенограмму с одним пиком от 0,3 до примерно 3,5° при 2;
b) взаимодействие исходного сырья, содержащего органическое соединение, в условиях реакции с упомянутым катализатором, при этом способ обработки выбирают из группы, состоящей из алкилирования, ацилирования, олигомеризации, селективного окисления, гидроочистки, изомеризации, деметаллирования, каталитической депарафинизации, гидроксилирования, гидрирования, аммоксимирования, дегидрирования, процесса Фишера-Тропша, крекинга и адсорбции.
2. Способ по п.1, в котором способ обработки представляет собой алкилирование, и в котором исходное сырье, содержащее органическое соединение, содержит ароматическое соединение либо алкан и алкилирующий агент.
3. Способ по п.2, в котором ароматическое соединение выбрано из группы, состоящей из бензола, нафталина, фенантрена, толуола, ксилола, изо-пропилнафталина, дифенилоксида и 2,4-ди-трет-бутилфенола.
4. Способ по п.3, в котором алкилирующий агент представляет собой олефин или спирт.
5. Способ по п.4, в котором, по меньшей мере, один гетероатом представляет собой Al и/или Ga.
6. Способ по п.5, в котором ароматическое соединение представляет собой нафталин или бензол и олефин представляет собой 1-гексадецен или этилен.
7. Способ по п.3, в котором алкилирующий агент представляет собой органический галогенид и в котором, по меньшей мере, один гетероатом выбран из группы, состоящей из Sn, Ga, Fe и их комбинаций.
8. Способ по п.7, в котором ароматическое соединение представляет собой бензол и органический галогенид представляет собой хлорбензол.
9. Способ по п.1, в котором способ обработки представляет собой селективное окисление, исходное сырье включает в себя окисляющий агент и, по меньшей мере, один гетероатом, выбранный из группы, состоящей из Cu, Zn, Fe, Ti, V, Sn, Mn, Cr, Mo и их комбинаций.
10. Способ по п.9, в котором, по меньшей мере, один гетероатом включает в себя, по меньшей мере, один атом, выбранный из группы, состоящей из Ti, Cr и Mo, исходное сырье включает в себя этилбензол, и в котором продукт, полученный в процессе селективного окисления, включает в себя ацетофенон.
11. Способ по п.9, в котором исходное сырье включает в себя спирт и, по меньшей мере, один гетероатом включает в себя Cu и/или Zn.
12. Способ по п.9, в котором органическое исходное сырье включает в себя циклогексанол, а продукт, получаемый в процессе селективного окисления, включает в себя циклогексанон.
13. Способ по п.1, в котором способ обработки представляет собой олигомеризацию, исходное сырье содержит, по меньшей мере, один олефин и, по меньшей мере, один гетероатом, выбранный из группы, состоящей из Al, Cr, Ga, Fe и их комбинаций.
14. Способ по п.13, в котором органическое исходное сырье включает в себя 1-децен и, по меньшей мере, один гетероатом включает в себя Al.
15. Способ по п.1, в котором способ обработки представляет собой ацилирование, исходное сырье содержит, по меньшей мере, одно ароматическое соединение и, по меньшей мере, один ацилирующий агент и, по меньшей мере, один гетероатом выбран из Al, Fe, Ga, In и их комбинаций.
16. Способ по п.15, в котором исходное сырье включает в себя 2-метоксинафталин и уксусный ангидрид.
17. Способ по п.1, в котором способ обработки включает в себя гидроочистку и, по меньшей мере, один гетероатом выбран из группы, состоящей из Ni, Mo, Co, W, Pt, Pd и их комбинаций.
18. Способ по п.17, в котором органическое исходное сырье включает в себя горючий сланец, или производную угольную жидкость, или остаточные нефтяные фракции, гидроочистка включает в себя один или несколько процессов из числа деазотирования, десульфирования, КУО-восстановления и деметаллирования.
19. Способ по п.18, в котором деметаллирование включает в себя удаление железа, никеля, меди, ванадия и мышьяка.
20. Способ по п.19, в котором исходное сырье представляет собой нефтяной остаток, гидроочистка включает в себя один или несколько процессов из числа деазотирования, десульфирования, деметаллирования и КУО-восстановления.
21. Способ по п.1, в котором способ обработки включает в себя крекинг.
22. Способ по п.21, в котором крекинг представляет собой гидрокрекинг и, по меньшей мере, один гетероатом включает в себя один или несколько металлов, выбранных из группы, состоящей из Ni, W, Mo, Co, Al и Ga.
23. Способ по п.20, в котором крекинг представляет собой каталитический крекинг и, по меньшей мере, один гетероатом включает в себя Al.
24. Способ по п.1, в котором способ обработки представляет собой каталитическую депарафинизацию и, по меньшей мере, один гетероатом включает в себя, по меньшей мере, один атом, выбранный из группы, состоящей из Al, Pt и Pd.
25. Способ по п.1, в котором способ обработки представляет собой гидроксилирование, по меньшей мере, один гетероатом выбран из группы, состоящей из Ti, Fe, Cu, Co, V, Cr и их комбинаций.
26. Способ по п.25, в котором исходное сырье содержит фенол и/или нафтол.
27. Способ по п.1, в котором способ обработки представляет собой изомеризацию и, по меньшей мере, один гетероатом выбран из группы, состоящей из Pd, Pt, Ni, Zr, W, Ga, Fe, Ti, Al и их комбинаций.
28. Способ по п.27, в котором исходное сырье включает в себя, по меньшей мере, один углеводород, выбранный из группы, состоящей из н-бутана, н-пентана, 1-бутена, ксилола и парафинистого нефтяного потока со средним числом атомов углерода большим, чем 20.
29. Способ по п.1, в котором способ обработки представляет собой дегидрирование и, по меньшей мере, один гетероатом выбран из группы, состоящей из V, Fe, Ga, Co, Cr и их комбинаций.
30. Способ по п.29, в котором исходное сырье включает в себя один или несколько насыщенных углеводородов.
31. Способ по п.29, в котором исходное сырье содержит один или несколько углеводородов, выбранных из группы, состоящей из пропана, изобутана и этилбензола.
32. Способ по п.1, в котором способ обработки представляет собой способ Фишера-Тропша и, по меньшей мере, один гетероатом выбран из группы, состоящей из Fe, Co, Ni и Ru и их сочетаний.
33. Способ по п.1, в котором катализатор взаимодействует с исходным сырьем, содержащим водород и монооксид углерода, при условиях: давление от примерно 5 до примерно 60 бар, предпочтительно от 8 до примерно 30 бар, ЧОСП от примерно 100 до примерно 10000 ч-1, предпочтительно от 300 ч-1 до примерно 2000 ч-1, температура от примерно 160 до примерно 300°С, предпочтительно от примерно 190 до примерно 260°С.
34. Способ по п.1, в котором композиция дополнительно включает в себя цеолит.
35. Каталитический материал, содержащий по существу мезопористую структуру, образованную одним или несколькими материалами, выбранными из группы, состоящей из диоксида кремния, оксида алюминия, диоксида титана, оксида хрома (III), оксида железа, диоксида молибдена, причем указанная мезопористая структура содержит, по меньшей мере, 97 об.% пор, имеющих размер пор в интервале от примерно 15 до примерно 300 Е, и имеет объем микропор, по меньшей мере, примерно 0,01 см3/г, и имеет площадь поверхности от 300 до примерно 1100 м2/г, и где мезопористая структура имеет введенный в нее, по меньшей мере, один каталитически и/или химически активный гетероатом, выбранный из группы, состоящей из Al, Ti, V, Cr, Zn, Fe, Sn, Mo, Ga, Ni, Co, In, Zr, Mn, Cu, Mg, Pd, Ru, W и их комбинаций в количестве, по меньшей мере, примерно 0,02 мас.%, причем упомянутый катализатор имеет рентгенограмму с одним пиком от 0,3° до примерно 3,5° при 2.
36. Каталитический материал по п.35, содержащий по существу мезопористую структуру, образованную одним или несколькими материалами, выбранными из группы, состоящей из диоксида кремния, оксида алюминия, диоксида титана, оксида хрома, оксида железа, диоксида молибдена, причем указанная мезопористая структура содержит, по меньшей мере, 97 об.% пор, имеющих размер пор в интервале от примерно 15 до примерно 300 Е и имеет дополнительно содержащий связующее вещество, выбранное из группы, состоящей из диоксида кремния, оксида алюминия, глины и их комбинации.
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KR20220071674A (ko) * | 2020-11-24 | 2022-05-31 | 현대자동차주식회사 | 표면처리 용액, 표면처리 용액의 제조방법, 표면처리 용액을 이용하여 활물질을 제조하는 방법 및 이를 통해 제조된 활물질 |
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- 2003-12-03 TW TW092134057A patent/TWI308506B/zh not_active IP Right Cessation
- 2003-12-03 BR BR0316981-2A patent/BR0316981A/pt not_active Application Discontinuation
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AU2003298790A1 (en) | 2004-06-30 |
IN2005MU00446A (ru) | 2005-10-07 |
US6930219B2 (en) | 2005-08-16 |
US20050201920A1 (en) | 2005-09-15 |
MX259239B (en) | 2008-08-01 |
BR0316981A (pt) | 2005-10-25 |
US20030188991A1 (en) | 2003-10-09 |
TWI308506B (en) | 2009-04-11 |
CN100441296C (zh) | 2008-12-10 |
EP1569750A1 (en) | 2005-09-07 |
AU2003298790B2 (en) | 2008-06-19 |
CA2508443A1 (en) | 2004-06-24 |
IN202747B (ru) | 2007-04-13 |
CN1720098A (zh) | 2006-01-11 |
CA2508443C (en) | 2011-05-17 |
MXPA05005461A (es) | 2005-07-25 |
WO2004052537A1 (en) | 2004-06-24 |
TW200424011A (en) | 2004-11-16 |
KR20050084122A (ko) | 2005-08-26 |
JP2006515584A (ja) | 2006-06-01 |
RU2334554C2 (ru) | 2008-09-27 |
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