NO330305B1 - Fremgangsmate for selektiv undertrykking av hydrogeneringsaktiviteten for en sulfidert katalysator - Google Patents
Fremgangsmate for selektiv undertrykking av hydrogeneringsaktiviteten for en sulfidert katalysator Download PDFInfo
- Publication number
- NO330305B1 NO330305B1 NO20044315A NO20044315A NO330305B1 NO 330305 B1 NO330305 B1 NO 330305B1 NO 20044315 A NO20044315 A NO 20044315A NO 20044315 A NO20044315 A NO 20044315A NO 330305 B1 NO330305 B1 NO 330305B1
- Authority
- NO
- Norway
- Prior art keywords
- catalyst
- activity
- treatment
- heteroatom
- selective
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims description 141
- 230000000694 effects Effects 0.000 title claims description 108
- 238000005984 hydrogenation reaction Methods 0.000 title claims description 52
- 238000000034 method Methods 0.000 title claims description 49
- 230000008569 process Effects 0.000 title claims description 33
- 125000005842 heteroatom Chemical group 0.000 claims description 88
- 238000011282 treatment Methods 0.000 claims description 80
- 239000003223 protective agent Substances 0.000 claims description 44
- 239000001257 hydrogen Substances 0.000 claims description 34
- 229910052739 hydrogen Inorganic materials 0.000 claims description 34
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 31
- 150000002430 hydrocarbons Chemical class 0.000 claims description 31
- 230000003197 catalytic effect Effects 0.000 claims description 26
- 229930195733 hydrocarbon Natural products 0.000 claims description 26
- 239000003795 chemical substances by application Substances 0.000 claims description 24
- 239000004215 Carbon black (E152) Substances 0.000 claims description 21
- 150000001336 alkenes Chemical class 0.000 claims description 21
- 229910052751 metal Inorganic materials 0.000 claims description 19
- 239000002184 metal Substances 0.000 claims description 19
- 230000002829 reductive effect Effects 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 15
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical group NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 claims description 14
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 11
- 150000001875 compounds Chemical class 0.000 claims description 10
- 150000001412 amines Chemical class 0.000 claims description 9
- 230000036961 partial effect Effects 0.000 claims description 9
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 8
- 150000001993 dienes Chemical class 0.000 claims description 6
- -1 olefin compounds Chemical class 0.000 claims description 6
- 239000002131 composite material Substances 0.000 claims description 4
- 229910044991 metal oxide Inorganic materials 0.000 claims description 3
- 150000004706 metal oxides Chemical class 0.000 claims description 3
- 150000001491 aromatic compounds Chemical class 0.000 claims 1
- 239000007789 gas Substances 0.000 description 37
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 26
- 229910052717 sulfur Inorganic materials 0.000 description 24
- 239000011593 sulfur Substances 0.000 description 24
- 238000006243 chemical reaction Methods 0.000 description 20
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 14
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 238000011065 in-situ storage Methods 0.000 description 12
- 238000006477 desulfuration reaction Methods 0.000 description 10
- 230000023556 desulfurization Effects 0.000 description 10
- 230000009849 deactivation Effects 0.000 description 9
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 8
- 238000011084 recovery Methods 0.000 description 8
- 230000005764 inhibitory process Effects 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- 241000899793 Hypsophrys nicaraguensis Species 0.000 description 6
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 6
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 238000009835 boiling Methods 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 230000009467 reduction Effects 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 229910001868 water Inorganic materials 0.000 description 6
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 5
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 5
- 229910052794 bromium Inorganic materials 0.000 description 5
- 238000007327 hydrogenolysis reaction Methods 0.000 description 5
- 229910052750 molybdenum Inorganic materials 0.000 description 5
- 229910000510 noble metal Inorganic materials 0.000 description 5
- 239000012808 vapor phase Substances 0.000 description 5
- 125000003118 aryl group Chemical group 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 230000002401 inhibitory effect Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 150000002894 organic compounds Chemical class 0.000 description 4
- 229910052763 palladium Inorganic materials 0.000 description 4
- 229910052697 platinum Inorganic materials 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 238000010504 bond cleavage reaction Methods 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 238000004939 coking Methods 0.000 description 3
- 238000011066 ex-situ storage Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910052759 nickel Inorganic materials 0.000 description 3
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000001588 bifunctional effect Effects 0.000 description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 230000000670 limiting effect Effects 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000011733 molybdenum Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 150000003464 sulfur compounds Chemical class 0.000 description 2
- 229910052721 tungsten Inorganic materials 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000003776 cleavage reaction Methods 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
- WHDPTDWLEKQKKX-UHFFFAOYSA-N cobalt molybdenum Chemical compound [Co].[Co].[Mo] WHDPTDWLEKQKKX-UHFFFAOYSA-N 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 125000003454 indenyl group Chemical class C1(C=CC2=CC=CC=C12)* 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- DDTIGTPWGISMKL-UHFFFAOYSA-N molybdenum nickel Chemical compound [Ni].[Mo] DDTIGTPWGISMKL-UHFFFAOYSA-N 0.000 description 1
- 150000002898 organic sulfur compounds Chemical class 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- HJWLCRVIBGQPNF-UHFFFAOYSA-N prop-2-enylbenzene Chemical class C=CCC1=CC=CC=C1 HJWLCRVIBGQPNF-UHFFFAOYSA-N 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000003079 shale oil Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 238000005486 sulfidation Methods 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
-
- 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
- C10G45/10—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 platinum group 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
- 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
- B01J23/84—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
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/16—Reducing
- B01J37/18—Reducing with gases containing free hydrogen
-
- 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
-
- 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
-
- 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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/20—Sulfiding
-
- 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
- C10G2400/02—Gasoline
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US36427502P | 2002-03-13 | 2002-03-13 | |
| US10/375,812 US7074735B2 (en) | 2002-03-13 | 2003-02-27 | Selectively suppressing catalytic hydrogenation |
| PCT/US2003/007205 WO2003078063A1 (en) | 2002-03-13 | 2003-03-11 | Selectively suppressing catalytic hydrogenation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| NO20044315L NO20044315L (no) | 2004-11-29 |
| NO330305B1 true NO330305B1 (no) | 2011-03-28 |
Family
ID=28045386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO20044315A NO330305B1 (no) | 2002-03-13 | 2004-10-12 | Fremgangsmate for selektiv undertrykking av hydrogeneringsaktiviteten for en sulfidert katalysator |
Country Status (9)
| Country | Link |
|---|---|
| US (2) | US7074735B2 (de) |
| EP (1) | EP1509322B1 (de) |
| JP (1) | JP4585763B2 (de) |
| AU (1) | AU2003220117B2 (de) |
| CA (1) | CA2477597C (de) |
| DE (1) | DE60328488D1 (de) |
| ES (1) | ES2329780T3 (de) |
| NO (1) | NO330305B1 (de) |
| WO (1) | WO2003078063A1 (de) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7776784B2 (en) * | 2003-07-14 | 2010-08-17 | Nippon Oil Corporation | Hydrodesulfurization catalyst and hydrodesulfurization process for gasoline fractions |
| US7988848B2 (en) * | 2005-04-15 | 2011-08-02 | Exxonmobil Research And Engineering Company | Activating hydroprocessing catalysts using carbon monoxide and use of catalysts for hydroprocessing |
| US20060234860A1 (en) * | 2005-04-15 | 2006-10-19 | Brignac Garland B | Activating hydroprocessing catalysts using carbon monoxide |
| CA2772061A1 (en) * | 2009-09-11 | 2011-03-17 | Exxonmobil Research And Engineering Company | Selective desulfurization of naphtha using reaction inhibitors |
| US20120000820A1 (en) * | 2010-06-30 | 2012-01-05 | Conocophillips Company | Hydroprocessing process for the improvement of the catalyst life |
| US8932453B2 (en) | 2010-07-23 | 2015-01-13 | Phillips 66 Company | Hydroprocessing process with improved catalyst activity |
| US8894844B2 (en) * | 2011-03-21 | 2014-11-25 | Exxonmobil Research And Engineering Company | Hydroprocessing methods utilizing carbon oxide-tolerant catalysts |
| CN113908888B (zh) * | 2020-07-09 | 2024-10-01 | 中国石油天然气股份有限公司 | 一种重油加氢催化剂的预硫化方法、重油加氢预硫化催化剂 |
Family Cites Families (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4978702A (de) * | 1972-12-04 | 1974-07-30 | ||
| US4020119A (en) * | 1973-08-23 | 1977-04-26 | Phillips Petroleum Company | Selective hydrogenation process |
| US4314901A (en) * | 1980-07-15 | 1982-02-09 | Phillips Petroleum Company | Catalytic hydrodesulfurization of an organic sulfur compound contained in gasoline |
| US4522709A (en) * | 1984-08-27 | 1985-06-11 | Phillips Petroleum Company | Catalytic hydrodesulfurization or hydrodenitrogenation |
| US4740491A (en) * | 1985-01-16 | 1988-04-26 | Gas Research Institute | Process for passivating high activity transition metal sulfide catalysts |
| US4828675A (en) * | 1987-12-04 | 1989-05-09 | Exxon Research And Engineering Company | Process for the production of ultra high octane gasoline, and other fuels from aromatic distillates |
| US4990242A (en) * | 1989-06-14 | 1991-02-05 | Exxon Research And Engineering Company | Enhanced sulfur removal from fuels |
| US5062943A (en) * | 1990-10-04 | 1991-11-05 | Mobil Oil Corporation | Modification of bifunctional catalyst activity in hydroprocessing |
| US5352354A (en) * | 1991-08-15 | 1994-10-04 | Mobil Oil Corporation | Gasoline upgrading process |
| US5212128A (en) * | 1991-11-29 | 1993-05-18 | Exxon Research & Engineering Company | Method for recovering or maintaining the activity of hydroisomerization catalysts |
| US5217935A (en) * | 1992-05-01 | 1993-06-08 | Abb Lummus Crest Inc. | Processes for regenerating catalysts contaminated with carbonaceous materials |
| US5286373A (en) * | 1992-07-08 | 1994-02-15 | Texaco Inc. | Selective hydrodesulfurization of naphtha using deactivated hydrotreating catalyst |
| US5423975A (en) * | 1992-07-08 | 1995-06-13 | Texaco Inc. | Selective hydrodesulfurization of naphtha using spent resid catalyst |
| US5525211A (en) * | 1994-10-06 | 1996-06-11 | Texaco Inc. | Selective hydrodesulfurization of naphtha using selectively poisoned hydroprocessing catalyst |
| FR2725381B1 (fr) * | 1994-10-07 | 1996-12-13 | Eurecat Europ Retrait Catalys | Procede de pretraitement hors site d'un catalyseur de traitement d'hydrocarbures |
| JP3291164B2 (ja) * | 1995-06-02 | 2002-06-10 | 日石三菱株式会社 | 接触分解ガソリンの脱硫方法 |
| US5763677A (en) * | 1995-12-06 | 1998-06-09 | Union Carbide Chemicals & Plastics Technology Corporation | Hydroformylation processes |
| US6231754B1 (en) * | 1996-02-02 | 2001-05-15 | Exxon Research And Engineering Company | High temperature naphtha desulfurization using a low metal and partially deactivated catalyst |
| JP3729621B2 (ja) * | 1997-09-24 | 2005-12-21 | 新日本石油株式会社 | 接触分解ガソリンの水素化脱硫方法及びガソリン |
| US5985136A (en) * | 1998-06-18 | 1999-11-16 | Exxon Research And Engineering Co. | Two stage hydrodesulfurization process |
| US6083379A (en) * | 1998-07-14 | 2000-07-04 | Phillips Petroleum Company | Process for desulfurizing and aromatizing hydrocarbons |
| US6228254B1 (en) * | 1999-06-11 | 2001-05-08 | Chevron U.S.A., Inc. | Mild hydrotreating/extraction process for low sulfur gasoline |
| JP2003027070A (ja) * | 2001-07-12 | 2003-01-29 | Idemitsu Kosan Co Ltd | 分解ガソリン留分の脱硫方法 |
-
2003
- 2003-02-27 US US10/375,812 patent/US7074735B2/en not_active Expired - Lifetime
- 2003-03-11 CA CA2477597A patent/CA2477597C/en not_active Expired - Fee Related
- 2003-03-11 JP JP2003576109A patent/JP4585763B2/ja not_active Expired - Fee Related
- 2003-03-11 WO PCT/US2003/007205 patent/WO2003078063A1/en active Search and Examination
- 2003-03-11 DE DE60328488T patent/DE60328488D1/de not_active Expired - Fee Related
- 2003-03-11 EP EP03716410A patent/EP1509322B1/de not_active Expired - Lifetime
- 2003-03-11 ES ES03716410T patent/ES2329780T3/es not_active Expired - Lifetime
- 2003-03-11 AU AU2003220117A patent/AU2003220117B2/en not_active Expired - Fee Related
-
2004
- 2004-10-12 NO NO20044315A patent/NO330305B1/no not_active IP Right Cessation
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2005
- 2005-09-22 US US11/234,668 patent/US7612012B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| AU2003220117B2 (en) | 2008-05-29 |
| ES2329780T3 (es) | 2009-12-01 |
| NO20044315L (no) | 2004-11-29 |
| US20030220186A1 (en) | 2003-11-27 |
| US20060019826A1 (en) | 2006-01-26 |
| AU2003220117A1 (en) | 2003-09-29 |
| JP4585763B2 (ja) | 2010-11-24 |
| JP2005520019A (ja) | 2005-07-07 |
| EP1509322A1 (de) | 2005-03-02 |
| EP1509322B1 (de) | 2009-07-22 |
| US7074735B2 (en) | 2006-07-11 |
| CA2477597A1 (en) | 2003-09-25 |
| WO2003078063A1 (en) | 2003-09-25 |
| DE60328488D1 (de) | 2009-09-03 |
| CA2477597C (en) | 2011-01-04 |
| US7612012B2 (en) | 2009-11-03 |
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