JP2023535563A - 炭化水素油のためのusyおよびベータゼオライトを含有する水素化分解触媒、並びに水素化分解触媒で炭化水素油を水素化分解する方法 - Google Patents
炭化水素油のためのusyおよびベータゼオライトを含有する水素化分解触媒、並びに水素化分解触媒で炭化水素油を水素化分解する方法 Download PDFInfo
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- JP2023535563A JP2023535563A JP2023503172A JP2023503172A JP2023535563A JP 2023535563 A JP2023535563 A JP 2023535563A JP 2023503172 A JP2023503172 A JP 2023503172A JP 2023503172 A JP2023503172 A JP 2023503172A JP 2023535563 A JP2023535563 A JP 2023535563A
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- zeolite
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- 239000003054 catalyst Substances 0.000 title claims abstract description 154
- 238000000034 method Methods 0.000 title claims abstract description 47
- 238000004517 catalytic hydrocracking Methods 0.000 title claims abstract description 45
- 230000008569 process Effects 0.000 title claims abstract description 28
- 150000002430 hydrocarbons Chemical class 0.000 title claims description 39
- 229930195733 hydrocarbon Natural products 0.000 title claims description 38
- 239000004215 Carbon black (E152) Substances 0.000 title claims description 37
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- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 163
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 163
- 239000000203 mixture Substances 0.000 claims abstract description 84
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical group [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000010936 titanium Substances 0.000 claims abstract description 34
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical group [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 33
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 33
- 229910052726 zirconium Chemical group 0.000 claims abstract description 33
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract description 23
- 229910052751 metal Inorganic materials 0.000 claims abstract description 20
- 239000002184 metal Substances 0.000 claims abstract description 20
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 31
- 239000001257 hydrogen Substances 0.000 claims description 30
- 229910052739 hydrogen Inorganic materials 0.000 claims description 30
- 239000013078 crystal Substances 0.000 claims description 26
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 12
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 10
- 229910052987 metal hydride Inorganic materials 0.000 claims description 10
- 150000004681 metal hydrides Chemical class 0.000 claims description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 8
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 8
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 8
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 6
- 238000009835 boiling Methods 0.000 claims description 6
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- 239000011733 molybdenum Substances 0.000 claims description 6
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- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 5
- 229910052721 tungsten Inorganic materials 0.000 claims description 5
- 239000010937 tungsten Substances 0.000 claims description 5
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims description 4
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- 229910052804 chromium Inorganic materials 0.000 claims description 4
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- 239000010941 cobalt Substances 0.000 claims description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 4
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- 229910052802 copper Inorganic materials 0.000 claims description 4
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- 229910052737 gold Inorganic materials 0.000 claims description 4
- 239000010931 gold Substances 0.000 claims description 4
- 229910052741 iridium Inorganic materials 0.000 claims description 4
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 229910052762 osmium Inorganic materials 0.000 claims description 4
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 claims description 4
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- 229910052697 platinum Inorganic materials 0.000 claims description 4
- 229910052703 rhodium Inorganic materials 0.000 claims description 4
- 239000010948 rhodium Substances 0.000 claims description 4
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims description 4
- 229910052707 ruthenium Inorganic materials 0.000 claims description 4
- 235000012239 silicon dioxide Nutrition 0.000 claims description 4
- 229910052709 silver Inorganic materials 0.000 claims description 4
- 239000004332 silver Substances 0.000 claims description 4
- 229910052682 stishovite Inorganic materials 0.000 claims description 4
- 229910052905 tridymite Inorganic materials 0.000 claims description 4
- 229910001845 yogo sapphire Inorganic materials 0.000 claims description 4
- 239000011148 porous material Substances 0.000 description 20
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
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- 230000007423 decrease Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
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- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 6
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- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
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- 229910052809 inorganic oxide Inorganic materials 0.000 description 6
- 238000006467 substitution reaction Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 4
- 238000012986 modification Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
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- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical compound [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
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- 238000007655 standard test method Methods 0.000 description 3
- 150000003609 titanium compounds Chemical class 0.000 description 3
- 238000004846 x-ray emission Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 2
- 238000005481 NMR spectroscopy Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 238000004231 fluid catalytic cracking Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 238000002371 ultraviolet--visible spectrum Methods 0.000 description 2
- 238000001392 ultraviolet--visible--near infrared spectroscopy Methods 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000002159 adsorption--desorption isotherm Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
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- 239000000969 carrier Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003979 granulating agent Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 150000002898 organic sulfur compounds Chemical class 0.000 description 1
- DCKVFVYPWDKYDN-UHFFFAOYSA-L oxygen(2-);titanium(4+);sulfate Chemical compound [O-2].[Ti+4].[O-]S([O-])(=O)=O DCKVFVYPWDKYDN-UHFFFAOYSA-L 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
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- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229910000348 titanium sulfate Inorganic materials 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 238000013519 translation Methods 0.000 description 1
- 230000014616 translation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 150000003755 zirconium compounds Chemical class 0.000 description 1
- ZXAUZSQITFJWPS-UHFFFAOYSA-J zirconium(4+);disulfate Chemical compound [Zr+4].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZXAUZSQITFJWPS-UHFFFAOYSA-J 0.000 description 1
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- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
-
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/18—Crystalline alumino-silicate carriers the catalyst containing platinum group metals or compounds thereof
-
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
- B01J2229/183—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself in framework positions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
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Abstract
Description
a=b≠c
α=β=γ=90°
があり、式中、aは、Åで表されるhに関する単位格子寸法であり、bは、Åで表されるkに関する単位格子寸法であり、cは、Åで表されるlに関する単位格子寸法である。ベータゼオライトの結晶格子定数は、以下の等式:
TiZr-USYゼオライトを、その全ての内容がここに引用される、米国特許第10293332号明細書に記載されているように調製した。
5質量%のTiZr-ベータゼオライト、25質量%のTiZr-USYゼオライト、および70質量%のアルミナのみの結合剤を使用して、触媒組成物1を配合した。30質量%のTiZr-USYゼオライトおよび70質量%のアルミナのみの結合剤を使用して、触媒組成物2を配合した。この組み合わされたTiZr-USYゼオライトと結合剤を、「担体」と称する。触媒組成物の成分の濃度を規定する目的のために、触媒組成物1と触媒組成物2の両方について、ニッケルとモリブデンを含む水素化成分は、担体の成分として計算した。この水素化成分は、最終的な触媒組成物(触媒+金属)に関する濃度を与えるために、担体濃度に加えられている。例えば、100kgの担体および32kgの水素化成分を含有する触媒組成物は、全触媒組成物の24質量%で水素化成分を有することになるであろう。
真空軽油(VGO)供給物に関する水素化分解プロセスに、触媒組成物1と触媒組成物2の両方を使用した。VGOは、0.923g/cm3の密度、2.51質量%の硫黄含有量、および960ppmの窒素含有量を有していた。ナフサ分画は、C5カットポイントからの分画、すなわち、約32℃から145℃までの分画であると考えた。灯油分画は、145℃から260℃の分画であると考えた。軽油分画は、260℃から360℃の分画であると考えた。中間蒸留物分画は、145℃から360℃の分画であると考えた。未変換の底部分画は、360℃を上回る任意の分画であると考えた。
以下、本発明の好ましい実施形態を項分け記載する。
実施形態1
触媒組成物であって、
触媒担体、および
前記触媒担体上に配置された少なくとも1種類の水素化金属成分、
を含み、
前記触媒担体は、
チタンとジルコニウムで置換された骨格を有する少なくとも1種類の超安定Y型ゼオライト(TiZr-USYゼオライト)、および
チタンとジルコニウムで置換された骨格を有する少なくとも1種類のベータゼオライト(TiZr-ベータゼオライト)、
を含む、触媒組成物。
実施形態2
前記少なくとも1種類のTiZr-USYゼオライトおよび前記少なくとも1種類のTiZr-ベータゼオライトの各々が、酸化物基準で計算して、0.1質量%から5質量%のジルコニウムおよび0.1質量%から5質量%のチタンで独立して置換されている、実施形態1に記載の触媒組成物。
実施形態3
前記少なくとも1種類の水素化金属成分が、クロム、モリブデン、タングステン、鉄、コバルト、ニッケル、銅、ルテニウム、ロジウム、パラジウム、銀、オスミウム、イリジウム、白金、金、およびその2つ以上の組合せからなる群より選択される、実施形態1または2に記載の触媒組成物。
実施形態4
前記少なくとも1種類のTiZr-USYゼオライトが、2.43nmから2.45nmの結晶格子定数を有する、実施形態1から3いずれか1つに記載の触媒組成物。
実施形態5
前記少なくとも1種類のTiZr-USYゼオライトが、10から100のSiO 2 対Al 2 O 3 のモル比を有する、実施形態1から4いずれか1つに記載の触媒組成物。
実施形態6
前記少なくとも1種類の水素化金属成分が、前記触媒組成物の0.01質量%から40質量%を構成する、実施形態1から5いずれか1つに記載の触媒組成物。
実施形態7
前記触媒担体が、該担体の全ゼオライト含有量に基づいて、70質量%から99質量%のTiZr-USYゼオライトを含む、実施形態1から6いずれか1つに記載の触媒組成物。
実施形態8
前記触媒担体が、該担体の全ゼオライト含有量に基づいて、1質量%から30質量%のTiZr-ベータゼオライトを含む、実施形態1から7いずれか1つに記載の触媒組成物。
実施形態9
前記触媒担体が、合計で1質量%から80質量%のTiZr-USYゼオライトとTiZr-ベータゼオライトを含む、実施形態1から8いずれか1つに記載の触媒組成物。
実施形態10
炭化水素油を水素化分解する方法であって、
炭化水素油流を水素化分解するために、反応器内で少なくとも1種類の炭化水素油流を少なくとも1種類の水素化分解触媒組成物および水素と接触させる工程、
を含み、
前記水素化分解触媒組成物は、
触媒担体、および
前記触媒担体上に配置された少なくとも1種類の水素化金属成分、
を含み、
前記触媒担体は、
チタンとジルコニウムで置換された骨格を有する少なくとも1種類の超安定Y型ゼオライト(TiZr-USYゼオライト)、および
チタンとジルコニウムで置換された骨格を有する少なくとも1種類のベータゼオライト(TiZr-ベータゼオライト)、
を含む、方法。
実施形態11
前記反応器が、300℃から500℃の温度で作動する、実施形態10に記載の方法。
実施形態12
前記炭化水素油が、375℃から833℃の沸点を有する、実施形態10または11に記載の方法。
実施形態13
前記水素が、3.5MPaから35MPaの圧力で前記反応器に添加される、実施形態10から12いずれか1つに記載の方法。
実施形態14
前記反応器が、500Nm 3 /m 3 から2500Nm 3 /m 3 の水素/油比を有する、実施形態10から13いずれか1つに記載の方法。
実施形態15
前記反応器が、0.1毎時から10毎時の液空間速度を有する、実施形態10から14いずれか1つに記載の方法。
Claims (15)
- 触媒組成物であって、
触媒担体、および
前記触媒担体上に配置された少なくとも1種類の水素化金属成分、
を含み、
前記触媒担体は、
チタンとジルコニウムで置換された骨格を有する少なくとも1種類の超安定Y型ゼオライト(TiZr-USYゼオライト)、および
チタンとジルコニウムで置換された骨格を有する少なくとも1種類のベータゼオライト(TiZr-ベータゼオライト)、
を含む、触媒組成物。 - 前記少なくとも1種類のTiZr-USYゼオライトおよび前記少なくとも1種類のTiZr-ベータゼオライトの各々が、酸化物基準で計算して、0.1質量%から5質量%のジルコニウムおよび0.1質量%から5質量%のチタンで独立して置換されている、請求項1記載の触媒組成物。
- 前記少なくとも1種類の水素化金属成分が、クロム、モリブデン、タングステン、鉄、コバルト、ニッケル、銅、ルテニウム、ロジウム、パラジウム、銀、オスミウム、イリジウム、白金、金、およびその2つ以上の組合せからなる群より選択される、請求項1または2記載の触媒組成物。
- 前記少なくとも1種類のTiZr-USYゼオライトが、2.43nmから2.45nmの結晶格子定数を有する、請求項1から3いずれか1項記載の触媒組成物。
- 前記少なくとも1種類のTiZr-USYゼオライトが、10から100のSiO2対Al2O3のモル比を有する、請求項1から4いずれか1項記載の触媒組成物。
- 前記少なくとも1種類の水素化金属成分が、前記触媒組成物の0.01質量%から40質量%を構成する、請求項1から5いずれか1項記載の触媒組成物。
- 前記触媒担体が、該担体の全ゼオライト含有量に基づいて、70質量%から99質量%のTiZr-USYゼオライトを含む、請求項1から6いずれか1項記載の触媒組成物。
- 前記触媒担体が、該担体の全ゼオライト含有量に基づいて、1質量%から30質量%のTiZr-ベータゼオライトを含む、請求項1から7いずれか1項記載の触媒組成物。
- 前記触媒担体が、合計で1質量%から80質量%のTiZr-USYゼオライトとTiZr-ベータゼオライトを含む、請求項1から8いずれか1項記載の触媒組成物。
- 炭化水素油を水素化分解する方法であって、
炭化水素油流を水素化分解するために、反応器内で少なくとも1種類の炭化水素油流を少なくとも1種類の水素化分解触媒組成物および水素と接触させる工程、
を含み、
前記水素化分解触媒組成物は、
触媒担体、および
前記触媒担体上に配置された少なくとも1種類の水素化金属成分、
を含み、
前記触媒担体は、
チタンとジルコニウムで置換された骨格を有する少なくとも1種類の超安定Y型ゼオライト(TiZr-USYゼオライト)、および
チタンとジルコニウムで置換された骨格を有する少なくとも1種類のベータゼオライト(TiZr-ベータゼオライト)、
を含む、方法。 - 前記反応器が、300℃から500℃の温度で作動する、請求項10記載の方法。
- 前記炭化水素油が、375℃から833℃の沸点を有する、請求項10または11記載の方法。
- 前記水素が、3.5MPaから35MPaの圧力で前記反応器に添加される、請求項10から12いずれか1項記載の方法。
- 前記反応器が、500Nm3/m3から2500Nm3/m3の水素/油比を有する、請求項10から13いずれか1項記載の方法。
- 前記反応器が、0.1毎時から10毎時の液空間速度を有する、請求項10から14いずれか1項記載の方法。
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