CN100556993C - 加氢处理催化剂,其制备方法及其在烃纯化方法中的用途 - Google Patents
加氢处理催化剂,其制备方法及其在烃纯化方法中的用途 Download PDFInfo
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- CN100556993C CN100556993C CNB2004800022908A CN200480002290A CN100556993C CN 100556993 C CN100556993 C CN 100556993C CN B2004800022908 A CNB2004800022908 A CN B2004800022908A CN 200480002290 A CN200480002290 A CN 200480002290A CN 100556993 C CN100556993 C CN 100556993C
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- Prior art keywords
- catalyzer
- hydrocarbon
- compound
- catalyst
- reactor
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Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims abstract description 32
- 150000002430 hydrocarbons Chemical class 0.000 title claims abstract description 26
- 229930195733 hydrocarbon Natural products 0.000 title claims abstract description 25
- 239000004215 Carbon black (E152) Substances 0.000 title claims abstract description 23
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 238000007670 refining Methods 0.000 title claims abstract description 10
- 229910052751 metal Inorganic materials 0.000 claims abstract description 39
- 239000002184 metal Substances 0.000 claims abstract description 39
- 238000012986 modification Methods 0.000 claims abstract description 24
- 230000004048 modification Effects 0.000 claims abstract description 23
- -1 sulfoxide compound Chemical class 0.000 claims abstract description 16
- 125000004196 benzothienyl group Chemical group S1C(=CC2=C1C=CC=C2)* 0.000 claims abstract description 9
- 125000001174 sulfone group Chemical group 0.000 claims abstract description 5
- 230000003647 oxidation Effects 0.000 claims description 26
- 238000007254 oxidation reaction Methods 0.000 claims description 26
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 25
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 23
- 150000001875 compounds Chemical group 0.000 claims description 18
- 150000003457 sulfones Chemical class 0.000 claims description 16
- 239000005864 Sulphur Substances 0.000 claims description 15
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 14
- 229910052750 molybdenum Inorganic materials 0.000 claims description 14
- 239000011733 molybdenum Substances 0.000 claims description 14
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 13
- 238000005987 sulfurization reaction Methods 0.000 claims description 13
- 229910052759 nickel Inorganic materials 0.000 claims description 12
- CIHOLLKRGTVIJN-UHFFFAOYSA-N tert‐butyl hydroperoxide Chemical compound CC(C)(C)OO CIHOLLKRGTVIJN-UHFFFAOYSA-N 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 11
- 238000009835 boiling Methods 0.000 claims description 9
- 239000002994 raw material Substances 0.000 claims description 9
- 125000003118 aryl group Chemical group 0.000 claims description 8
- 229910052717 sulfur Inorganic materials 0.000 claims description 8
- 239000011593 sulfur Substances 0.000 claims description 8
- 239000010941 cobalt Substances 0.000 claims description 7
- 229910017052 cobalt Inorganic materials 0.000 claims description 7
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 7
- 150000003462 sulfoxides Chemical class 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- IYYZUPMFVPLQIF-UHFFFAOYSA-N dibenzothiophene Chemical compound C1=CC=C2C3=CC=CC=C3SC2=C1 IYYZUPMFVPLQIF-UHFFFAOYSA-N 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 6
- 150000004966 inorganic peroxy acids Chemical class 0.000 claims description 6
- 150000004967 organic peroxy acids Chemical class 0.000 claims description 6
- 229910052721 tungsten Inorganic materials 0.000 claims description 6
- UDKYUQZDRMRDOR-UHFFFAOYSA-N tungsten Chemical compound [W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W][W] UDKYUQZDRMRDOR-UHFFFAOYSA-N 0.000 claims description 6
- 239000010937 tungsten Substances 0.000 claims description 6
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 5
- OUUQCZGPVNCOIJ-UHFFFAOYSA-M Superoxide Chemical compound [O-][O] OUUQCZGPVNCOIJ-UHFFFAOYSA-M 0.000 claims description 5
- 238000012545 processing Methods 0.000 claims description 5
- 238000004073 vulcanization Methods 0.000 claims description 5
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 claims description 4
- YTPLMLYBLZKORZ-UHFFFAOYSA-N Thiophene Chemical compound C=1C=CSC=1 YTPLMLYBLZKORZ-UHFFFAOYSA-N 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 239000010779 crude oil Substances 0.000 claims description 4
- 230000008021 deposition Effects 0.000 claims description 4
- 239000002904 solvent Substances 0.000 claims description 4
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 3
- 125000001931 aliphatic group Chemical group 0.000 claims description 3
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 3
- 239000005077 polysulfide Substances 0.000 claims description 3
- 229920001021 polysulfide Polymers 0.000 claims description 3
- 150000008117 polysulfides Polymers 0.000 claims description 3
- 229960001866 silicon dioxide Drugs 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- FCEHBMOGCRZNNI-UHFFFAOYSA-N 1-benzothiophene Chemical compound C1=CC=C2SC=CC2=C1 FCEHBMOGCRZNNI-UHFFFAOYSA-N 0.000 claims description 2
- 238000011065 in-situ storage Methods 0.000 claims description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 2
- 239000012188 paraffin wax Substances 0.000 claims description 2
- 150000002978 peroxides Chemical class 0.000 claims description 2
- 229930192474 thiophene Natural products 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 239000003921 oil Substances 0.000 description 16
- 239000007789 gas Substances 0.000 description 15
- 238000006477 desulfuration reaction Methods 0.000 description 12
- 230000023556 desulfurization Effects 0.000 description 11
- 230000000694 effects Effects 0.000 description 11
- VLXBWPOEOIIREY-UHFFFAOYSA-N dimethyl diselenide Natural products C[Se][Se]C VLXBWPOEOIIREY-UHFFFAOYSA-N 0.000 description 9
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 8
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 238000004821 distillation Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 230000008929 regeneration Effects 0.000 description 5
- 238000011069 regeneration method Methods 0.000 description 5
- 238000004517 catalytic hydrocracking Methods 0.000 description 4
- 230000000875 corresponding effect Effects 0.000 description 4
- IKJFYINYNJYDTA-UHFFFAOYSA-N dibenzothiophene sulfone Chemical compound C1=CC=C2S(=O)(=O)C3=CC=CC=C3C2=C1 IKJFYINYNJYDTA-UHFFFAOYSA-N 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000005984 hydrogenation reaction Methods 0.000 description 2
- 230000000977 initiatory effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- HQALDKFFRYFTKP-UHFFFAOYSA-N 2-[4-[4-(2-benzyl-1-benzothiophen-3-yl)phenyl]-2-bromo-6-(3-methoxyphenyl)phenoxy]acetic acid Chemical compound COC1=CC=CC(C=2C(=C(Br)C=C(C=2)C=2C=CC(=CC=2)C=2C3=CC=CC=C3SC=2CC=2C=CC=CC=2)OCC(O)=O)=C1 HQALDKFFRYFTKP-UHFFFAOYSA-N 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- MCKLZLIIGNPIEJ-UHFFFAOYSA-N [S].N1N=CC=C1 Chemical compound [S].N1N=CC=C1 MCKLZLIIGNPIEJ-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 125000002877 alkyl aryl group Chemical group 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000005899 aromatization reaction Methods 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 150000004965 peroxy acids Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000009183 running Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- CWERGRDVMFNCDR-UHFFFAOYSA-N thioglycolic acid Chemical compound OC(=O)CS CWERGRDVMFNCDR-UHFFFAOYSA-N 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/12—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including oxidation as the refining step in the absence of hydrogen
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- B01J23/84—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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
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- B01J23/84—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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/882—Molybdenum and cobalt
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- B01J23/84—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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
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- 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
- B01J23/84—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 arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
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- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
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- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
- B01J31/34—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of chromium, molybdenum or tungsten
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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
- C10G27/00—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
- C10G27/04—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen
- C10G27/12—Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with oxygen or compounds generating oxygen with oxygen-generating compounds, e.g. per-compounds, chromic acid, chromates
-
- 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
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
- C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
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- B—PERFORMING OPERATIONS; TRANSPORTING
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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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
-
- 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
催化剂 | 处理 | 改性 | 硫化 |
A | 没有 | 没有 | GO<sub>1</sub>+2重量%DMDS |
B | 外部 | 单独GO<sub>1</sub> | GO<sub>1</sub>+2重量%DMDS |
C | 就地 | 单独GO<sub>1</sub> | GO<sub>1</sub>+2重量%DMDS |
D | 外部 | GO<sub>1</sub>+6.3重量%TBHP | GO<sub>1</sub>+2重量%DMDS |
E | 就地 | GO<sub>1</sub>+6.3重量%TBHP | GO<sub>1</sub>+2重量%DMDS |
F | 外部 | dBTS | GO<sub>1</sub>+2重量%DMDS |
G | 就地 | GO<sub>2</sub>+6.3重量%TBHP | GO<sub>1</sub>+2重量%DMDS |
原料类型 | 25%LCO-75%GO的混合物 | GO<sub>1</sub> | GO<sub>2</sub> |
硫(ppm) | 14 447 | 10 117 | 49 |
15℃的密度(g/ml) | 0.8684 | 0.8579 | 0.8501 |
单芳族化合物(重量%) | 18.7 | 14.8 | 28 |
二芳族化合物(重量%) | 14.8 | 13 | 5 |
三芳族化合物(重量%) | 2.8 | 1.6 | 1 |
总芳族化合物(重量%) | 36.3 | 29.4 | 34 |
氮(ppm) | 228 | 158 | 29.7 |
ASTM D86(℃)初始沸点5体积%10体积%20体积%30体积%40体积%50体积%60体积%70体积%80体积%90体积%95体积%最终沸点 | 203230244257268278289301314329347359363 | 244264273280286293299306314324339350352 | 201229241255266276287298311326347363365 |
压力 | 27×10<sup>5</sup>Pa |
HSV | 1h<sup>-1</sup> |
H<sub>2</sub>/油混合物比 | 130 S1/1 |
A | B | C | D | E | F | G |
T<sub>HDS</sub> | T<sub>HDS</sub>-1℃ | T<sub>HDS</sub>-2℃ | T<sub>HDS</sub>-19℃ | T<sub>HDS</sub>-18℃ | T<sub>HDS</sub>-15℃ | T<sub>HDS</sub>-19℃ |
T<sub>HDN</sub> | T<sub>HDN</sub>-2℃ | T<sub>HDN</sub>-3℃ | T<sub>HDN</sub>-28℃ | T<sub>HDN</sub>-26℃ | T<sub>HDN</sub>-20℃ | T<sub>HDN</sub>-27℃ |
A | G | G’ |
T<sub>HDS</sub> | T<sub>HDS</sub>-19℃ | T<sub>HDS</sub>-18℃ |
T<sub>HDN</sub> | T<sub>HDN</sub>-27℃ | T<sub>HDN</sub>-25℃ |
Claims (23)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR03/00439 | 2003-01-16 | ||
FR0300439A FR2850041B1 (fr) | 2003-01-16 | 2003-01-16 | Catalyseur d'hydrotraitement, son procede de preparation et son utilisation dans un procede de purification d'hydrocarbures. |
Publications (2)
Publication Number | Publication Date |
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CN1738889A CN1738889A (zh) | 2006-02-22 |
CN100556993C true CN100556993C (zh) | 2009-11-04 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CNB2004800022908A Expired - Lifetime CN100556993C (zh) | 2003-01-16 | 2004-01-15 | 加氢处理催化剂,其制备方法及其在烃纯化方法中的用途 |
Country Status (8)
Country | Link |
---|---|
US (1) | US7686947B2 (zh) |
EP (1) | EP1587897B1 (zh) |
JP (1) | JP4541352B2 (zh) |
KR (1) | KR101113294B1 (zh) |
CN (1) | CN100556993C (zh) |
DK (1) | DK1587897T3 (zh) |
FR (1) | FR2850041B1 (zh) |
WO (1) | WO2004067683A1 (zh) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4922783B2 (ja) * | 2006-02-24 | 2012-04-25 | コスモ石油株式会社 | 炭化水素用脱硫剤 |
EP2001802B1 (en) * | 2006-03-03 | 2021-06-09 | Saudi Arabian Oil Company | Catalytic process for deep oxidative desulfurization of liquid transportation fuels |
FR2910351B1 (fr) * | 2006-12-22 | 2009-02-27 | Total France Sa | Catalyseur d'hydrotraitement, son procede de preparation et son utilisation. |
US20090223868A1 (en) * | 2008-03-06 | 2009-09-10 | Opinder Kishan Bhan | Catalyst and process for the selective hydrodesulfurization of an olefin containing hydrocarbon feedstock |
WO2010100256A2 (en) | 2009-03-06 | 2010-09-10 | Albemarle Europe Sprl | Bulk sulfidic mixed metal catalyst and methods for its manufacture and use in converting syngas to alcohol |
US20110220550A1 (en) * | 2010-03-15 | 2011-09-15 | Abdennour Bourane | Mild hydrodesulfurization integrating targeted oxidative desulfurization to produce diesel fuel having an ultra-low level of organosulfur compounds |
US9296960B2 (en) | 2010-03-15 | 2016-03-29 | Saudi Arabian Oil Company | Targeted desulfurization process and apparatus integrating oxidative desulfurization and hydrodesulfurization to produce diesel fuel having an ultra-low level of organosulfur compounds |
US8926825B2 (en) * | 2010-03-19 | 2015-01-06 | Mark Cullen | Process for removing sulfur from hydrocarbon streams using hydrotreatment, fractionation and oxidation |
KR101816318B1 (ko) * | 2010-12-09 | 2018-01-12 | 에스케이이노베이션 주식회사 | 수소 처리 촉매 및 이의 제조방법 |
US8906227B2 (en) | 2012-02-02 | 2014-12-09 | Suadi Arabian Oil Company | Mild hydrodesulfurization integrating gas phase catalytic oxidation to produce fuels having an ultra-low level of organosulfur compounds |
US8920635B2 (en) | 2013-01-14 | 2014-12-30 | Saudi Arabian Oil Company | Targeted desulfurization process and apparatus integrating gas phase oxidative desulfurization and hydrodesulfurization to produce diesel fuel having an ultra-low level of organosulfur compounds |
JP6685317B2 (ja) * | 2014-11-06 | 2020-04-22 | シエル・インターナシヨナル・リサーチ・マートスハツペイ・ベー・ヴエー | 高活性および自己活性化特性を有する自己活性型水素化触媒と残油原料を処理するためのその使用 |
CN107297215B (zh) * | 2016-04-16 | 2019-08-06 | 中国石油化工股份有限公司 | 加氢处理催化剂及其制备方法 |
GB201615219D0 (en) | 2016-09-07 | 2016-10-19 | Vascutek Ltd And Univ Medical Center Hamburg-Eppendorf (Uke) | Hybrid prosthesis and delivery system |
KR20220012247A (ko) * | 2019-05-23 | 2022-02-03 | 에보닉 오퍼레이션스 게엠베하 | 황 저감에 사용하기 위한 재활성화된 수소화 처리 촉매 |
MX2022003972A (es) * | 2022-03-31 | 2023-10-02 | Mexicano Inst Petrol | Proceso para la activacion y arranque de catalizadores de hidrodesulfuracion profunda de destilados intermedios. |
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US3945914A (en) * | 1974-08-23 | 1976-03-23 | Atlantic Richfield Company | Process for "sulfur reduction of an oxidized hydrocarbon by forming a metal-sulfur-containing compound" |
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US3719589A (en) * | 1971-03-05 | 1973-03-06 | Texaco Inc | Asphalt separation in desulfurization with an oxidation step |
US3816301A (en) * | 1972-06-30 | 1974-06-11 | Atlantic Richfield Co | Process for the desulfurization of hydrocarbons |
FR2607145B1 (fr) * | 1986-11-25 | 1990-06-08 | Inst Francais Du Petrole | Procede ameliore de conversion thermique de fractions lourdes de petrole et de residus de raffinage, en presence de composes oxygenes du soufre, de l'azote ou du phosphore |
US5454933A (en) * | 1991-12-16 | 1995-10-03 | Exxon Research And Engineering Company | Deep desulfurization of distillate fuels |
FR2706326B1 (fr) * | 1993-06-14 | 1995-09-15 | Eurecat Europ Retrait Catalys | Nouveau mode de présulfuration de catalyseur. |
US5958224A (en) * | 1998-08-14 | 1999-09-28 | Exxon Research And Engineering Co | Process for deep desulfurization using combined hydrotreating-oxidation |
US6368495B1 (en) * | 1999-06-07 | 2002-04-09 | Uop Llc | Removal of sulfur-containing compounds from liquid hydrocarbon streams |
FR2818990B1 (fr) * | 2000-12-28 | 2004-09-24 | Total Raffinage Distribution | Procede et dispositif de desulfuration d'hydrocarbures charges en derives thiopheniques |
FR2820991B1 (fr) * | 2001-02-22 | 2003-10-03 | Atofina | Procede de sulfuration des catalyseurs d'hydrotraitement |
US20060226049A1 (en) * | 2005-04-08 | 2006-10-12 | Nemeth Laszlo T | Oxidative desulfurization of hydrocarbon fuels |
-
2003
- 2003-01-16 FR FR0300439A patent/FR2850041B1/fr not_active Expired - Lifetime
-
2004
- 2004-01-15 JP JP2006502101A patent/JP4541352B2/ja not_active Expired - Lifetime
- 2004-01-15 EP EP04702352.8A patent/EP1587897B1/fr not_active Expired - Lifetime
- 2004-01-15 KR KR1020057013219A patent/KR101113294B1/ko active IP Right Grant
- 2004-01-15 US US10/542,269 patent/US7686947B2/en active Active
- 2004-01-15 WO PCT/FR2004/000071 patent/WO2004067683A1/fr active Application Filing
- 2004-01-15 DK DK04702352.8T patent/DK1587897T3/da active
- 2004-01-15 CN CNB2004800022908A patent/CN100556993C/zh not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3945914A (en) * | 1974-08-23 | 1976-03-23 | Atlantic Richfield Company | Process for "sulfur reduction of an oxidized hydrocarbon by forming a metal-sulfur-containing compound" |
Also Published As
Publication number | Publication date |
---|---|
JP2006516222A (ja) | 2006-06-29 |
FR2850041A1 (fr) | 2004-07-23 |
US20060054537A1 (en) | 2006-03-16 |
US7686947B2 (en) | 2010-03-30 |
EP1587897B1 (fr) | 2014-03-12 |
KR20050090007A (ko) | 2005-09-09 |
KR101113294B1 (ko) | 2012-02-20 |
JP4541352B2 (ja) | 2010-09-08 |
DK1587897T3 (da) | 2014-06-16 |
CN1738889A (zh) | 2006-02-22 |
FR2850041B1 (fr) | 2006-07-07 |
EP1587897A1 (fr) | 2005-10-26 |
WO2004067683A1 (fr) | 2004-08-12 |
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