CA2485665A1 - Passivation de catalyseur d'hydroconversion sulfure - Google Patents
Passivation de catalyseur d'hydroconversion sulfure Download PDFInfo
- Publication number
- CA2485665A1 CA2485665A1 CA002485665A CA2485665A CA2485665A1 CA 2485665 A1 CA2485665 A1 CA 2485665A1 CA 002485665 A CA002485665 A CA 002485665A CA 2485665 A CA2485665 A CA 2485665A CA 2485665 A1 CA2485665 A1 CA 2485665A1
- Authority
- CA
- Canada
- Prior art keywords
- catalyst
- contact
- gas flow
- organic liquid
- oxygen
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract 10
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract 6
- 238000002161 passivation Methods 0.000 title claims abstract 3
- 239000005864 Sulphur Substances 0.000 title abstract 2
- 238000000034 method Methods 0.000 claims abstract 15
- 230000001590 oxidative effect Effects 0.000 claims abstract 6
- 239000007788 liquid Substances 0.000 claims abstract 5
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract 3
- 229930195733 hydrocarbon Natural products 0.000 claims abstract 3
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract 3
- 238000011282 treatment Methods 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 4
- 229910052760 oxygen Inorganic materials 0.000 claims 4
- 239000001301 oxygen Substances 0.000 claims 4
- 239000011593 sulfur Substances 0.000 claims 4
- 229910052717 sulfur Inorganic materials 0.000 claims 4
- 150000002894 organic compounds Chemical class 0.000 claims 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims 2
- 238000009835 boiling Methods 0.000 claims 2
- 150000002148 esters Chemical class 0.000 claims 2
- 150000001298 alcohols Chemical class 0.000 claims 1
- 150000001299 aldehydes Chemical class 0.000 claims 1
- 150000001408 amides Chemical class 0.000 claims 1
- 150000001412 amines Chemical class 0.000 claims 1
- 239000010775 animal oil Substances 0.000 claims 1
- 235000014113 dietary fatty acids Nutrition 0.000 claims 1
- 229930195729 fatty acid Natural products 0.000 claims 1
- 239000000194 fatty acid Substances 0.000 claims 1
- 150000004665 fatty acids Chemical class 0.000 claims 1
- 239000012530 fluid Substances 0.000 claims 1
- 125000005842 heteroatom Chemical group 0.000 claims 1
- 239000003350 kerosene Substances 0.000 claims 1
- 150000002576 ketones Chemical class 0.000 claims 1
- -1 mereaptans Chemical class 0.000 claims 1
- 229910052757 nitrogen Inorganic materials 0.000 claims 1
- 230000000630 rising effect Effects 0.000 claims 1
- 150000003457 sulfones Chemical class 0.000 claims 1
- 150000003568 thioethers Chemical class 0.000 claims 1
- 150000003626 triacylglycerols Chemical class 0.000 claims 1
- 239000008158 vegetable oil Substances 0.000 claims 1
- 235000013311 vegetables Nutrition 0.000 claims 1
- 239000001993 wax Substances 0.000 claims 1
- 238000011066 ex-situ storage Methods 0.000 abstract 1
Classifications
-
- 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
-
- 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
- B01J23/88—Molybdenum
- B01J23/883—Molybdenum and nickel
-
- 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
- B01J23/888—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
- B01J37/06—Washing
-
- 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
- B01J37/12—Oxidising
- B01J37/14—Oxidising with gases containing free oxygen
-
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
-
- 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
- B01J33/00—Protection of catalysts, e.g. by coating
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
- C10G2300/1014—Biomass of vegetal origin
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
- C10G2300/1018—Biomass of animal origin
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1051—Kerosene having a boiling range of about 180 - 230 °C
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °C
-
- 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
- C10G2300/10—Feedstock materials
- C10G2300/1074—Vacuum distillates
-
- 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
-
- 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
- C10G2300/70—Catalyst aspects
- C10G2300/705—Passivation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
La présente invention concerne un procédé de passivation oxydante hors site des catalyseurs d'hydroconversion d'hydrocarbures et notamment d'hydrotraitement dans leurs états sulfures, dans lequel le catalyseur sulfu ré est soumis à 2 traitements : mise en contact avec un flux gazeux oxydant, et mise en contact avec un liquide organique (hydrocarbure par exemple) qui remplit partiellement sa porosité.
Claims (14)
1. Procédé de passivation oxydante hors-site d'un catalyseur d'hydroconversion d'hydrocarbures caractérisé en ce que ledit catalyseur sulfuré est soumis à au moins deux traitements : mise en contact avec au moins un flux gazeux oxydant, et mise en contact avec au moins un liquide organique de point d'ébullition initial supérieur à
120°C qui remplit au moins partiellement la porosité du catalyseur.
120°C qui remplit au moins partiellement la porosité du catalyseur.
2. Procédé selon la revendication 1 dans lequel ledit catalyseur sulfuré est dans une première étape mis en contact avec au moins un flux gazeux oxydant et dans une deuxième étape mis au contact dudit liquide organique.
3. Procédé selon la revendication 1 dans lequel ledit catalyseur sulfuré est dans une première étape mis au contact dudit liquide organique et dans une deuxième étape mis en contact avec au moins un flux gazeux oxydant.
4. Procédé selon l'une des revendications 1 à 3 dans lequel la mise en contact avec ledit flux gazeux est effectuée en deux temps, le premier sous une pression partielle d'oxygène inférieure à 8 kPa, le second, sous une pression partielle en oxygène supérieure à celle du premier temps et au plus à 21.3kPa.
5. Procédé selon la revendication 4 dans lequel le deuxième temps de la première étape est effectué sous air.
6. Procédé selon la revendication 1 dans lequel la mise en contact avec ledit flux gazeux est effectuée en un ou plusieurs temps avec un ou des flux gazeux ayant tous une pression partielle en oxygène supérieure à 8 kPa.
7. Procédé selon la revendication 6 dans lequel ce ou ces flux sont de l'air.
8. Procédé selon l'une des revendications précédentes dans lequel le catalyseur est en mouvement.
9. Procédé selon la revendication 8 dans lequel le catalyseur est en lit mobile.
10. Procédé selon la revendication 9 mis en oeuvre dans un four rotatif, un four à lit fluide, un four à bande, un four à lit croulant ou un dispositif à lit ascendant.
11. Procédé selon l'une des revendications précédentes dans lequel ledit liquide organique utilisé en deuxième étape est choisi dans le groupe constitué par le kérosène, le gasoil, les distillats sous vide, une base huileuse, les cires et les paraffines de point d'ébullition initial supérieure à 180°C.
12. Procédé selon l'une des revendications précédentes dans lequel ledit composé organique contient au moins un hétéroatome choisi parmi l'oxygène, le soufre et l'azote.
13. Procédé selon la revendication 12 dans lequel ledit composé organique est choisi parmi les alcools, aldéhydes, cétones, esters, amines, amides, mereaptans, sulfures et sulfones.
14. Procédé selon la revendication 13 dans lequel le composé organique est un ester choisi de préférence parmi les huiles végétales ou animales, les triglycérides d' acides gras partiellement insaturés.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR03/01634 | 2003-02-11 | ||
FR0301634A FR2850882B1 (fr) | 2003-02-11 | 2003-02-11 | Passivation de catalyseur d'hydroconversion sulfure |
PCT/FR2004/000272 WO2004071655A1 (fr) | 2003-02-11 | 2004-02-06 | Passivation de catalyseur d'hydroconversion sulfure |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2485665A1 true CA2485665A1 (fr) | 2004-08-26 |
CA2485665C CA2485665C (fr) | 2011-09-27 |
Family
ID=32731959
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2485665A Expired - Lifetime CA2485665C (fr) | 2003-02-11 | 2004-02-06 | Passivation de catalyseur d'hydroconversion sulfure |
Country Status (7)
Country | Link |
---|---|
US (1) | US7582587B2 (fr) |
JP (1) | JP5016918B2 (fr) |
CA (1) | CA2485665C (fr) |
DE (1) | DE112004000001B4 (fr) |
FR (1) | FR2850882B1 (fr) |
LU (1) | LU91102B1 (fr) |
WO (1) | WO2004071655A1 (fr) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7407909B2 (en) * | 2004-10-01 | 2008-08-05 | Exxonmobil Research And Engineering Company | Ex-situ reduction and dry passivation of noble metal catalysts |
FR2880823B1 (fr) * | 2005-01-20 | 2008-02-22 | Total France Sa | Catalyseur d'hydrotraitement, son procede de preparation et et son utilisation |
FR2915908B1 (fr) * | 2007-05-10 | 2010-09-03 | Eurecat Sa | Procede de sulfuration ou presulfuration de particules solides d'un catalyseur ou d'un adsorbant |
US8519379B2 (en) | 2009-12-08 | 2013-08-27 | Zena Technologies, Inc. | Nanowire structured photodiode with a surrounding epitaxially grown P or N layer |
US8889455B2 (en) | 2009-12-08 | 2014-11-18 | Zena Technologies, Inc. | Manufacturing nanowire photo-detector grown on a back-side illuminated image sensor |
US8890271B2 (en) | 2010-06-30 | 2014-11-18 | Zena Technologies, Inc. | Silicon nitride light pipes for image sensors |
US8835831B2 (en) | 2010-06-22 | 2014-09-16 | Zena Technologies, Inc. | Polarized light detecting device and fabrication methods of the same |
US8269985B2 (en) | 2009-05-26 | 2012-09-18 | Zena Technologies, Inc. | Determination of optimal diameters for nanowires |
US8748799B2 (en) | 2010-12-14 | 2014-06-10 | Zena Technologies, Inc. | Full color single pixel including doublet or quadruplet si nanowires for image sensors |
US8735797B2 (en) | 2009-12-08 | 2014-05-27 | Zena Technologies, Inc. | Nanowire photo-detector grown on a back-side illuminated image sensor |
US9515218B2 (en) | 2008-09-04 | 2016-12-06 | Zena Technologies, Inc. | Vertical pillar structured photovoltaic devices with mirrors and optical claddings |
US9299866B2 (en) | 2010-12-30 | 2016-03-29 | Zena Technologies, Inc. | Nanowire array based solar energy harvesting device |
US8299472B2 (en) | 2009-12-08 | 2012-10-30 | Young-June Yu | Active pixel sensor with nanowire structured photodetectors |
CA2742549C (fr) | 2008-11-10 | 2017-07-04 | Institut National De La Recherche Scientifique | Precurseurs de catalyseurs, catalyseurs et leurs procedes de production |
MY166873A (en) * | 2011-12-16 | 2018-07-24 | Basf Corp | Protected reduced metal catalyst |
FR2994394B1 (fr) * | 2012-08-09 | 2015-08-21 | Eurecat Sa | Procede de passivation par un compose azote d'un catalyseur zeolitique, en particulier d'un catalyseur d'hydrocraquage |
CN113083376A (zh) * | 2019-12-23 | 2021-07-09 | 内蒙古伊泰煤基新材料研究院有限公司 | 一种加氢裂化催化剂的钝化方法 |
GB202100248D0 (en) * | 2021-01-08 | 2021-02-24 | Johnson Matthey Plc | Catalyst passivation method |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2905636A (en) * | 1957-06-27 | 1959-09-22 | Universal Oil Prod Co | Manufacture and use of supported molybdenum-containing catalysts |
US3838066A (en) * | 1971-10-01 | 1974-09-24 | Standard Oil Co | Method for stabilizing pyrophoric materials in a catalyst bed |
US5094991A (en) * | 1983-08-29 | 1992-03-10 | Chevron Research Company | Slurry catalyst for hydroprocessing heavy and refractory oils |
DE3562987D1 (en) | 1984-10-30 | 1988-07-07 | Eurecat Europ Retrait Catalys | Method for presulfiding a catalyst for the treatment of hydrocarbons |
FR2689420B1 (fr) * | 1992-04-01 | 1994-06-17 | Eurecat Europ Retrait Catalys | Procede de presulfuration de catalyseur de traitement d'hydrocarbures. |
CN1100617C (zh) | 1993-05-04 | 2003-02-05 | Cri国际有限公司 | 一种处理可自燃的催化剂的方法 |
US6093309A (en) * | 1993-05-04 | 2000-07-25 | Cri International, Inc. | Method of treating spontaneously combustible catalysts |
FR2725381B1 (fr) * | 1994-10-07 | 1996-12-13 | Eurecat Europ Retrait Catalys | Procede de pretraitement hors site d'un catalyseur de traitement d'hydrocarbures |
FR2743512B1 (fr) * | 1996-01-17 | 1998-03-13 | Eurecat Europ Retrait Catalys | Procede d'incorporation de soufre dans la porosite d'un catalyseur de traitement d'hydrocarbures |
FR2749779B1 (fr) * | 1996-06-12 | 1998-09-11 | Eurecat Europ Retrait Catalys | Procede de presulfuration de catalyseurs d'hydrotraitement |
US5922638A (en) * | 1996-06-12 | 1999-07-13 | Europeene De Retraitement De Catalyseurs Eurecat | Process for presulfurizing hydrotreatment catalysts |
US5958816A (en) * | 1997-02-28 | 1999-09-28 | Tricat, Inc. | Method of presulfiding and passivating a hydrocarbon conversion catalyst |
FR2767072B1 (fr) * | 1997-08-11 | 1999-09-10 | Eurecat Europ Retrait Catalys | Protection de catalyseurs par depot de couche protectrice |
FR2784312B1 (fr) * | 1998-10-12 | 2000-11-10 | Eurecat Europ Retrait Catalys | Presulfuration hors site en presence de molecule hydrocarbonee |
US6509291B2 (en) * | 2000-04-11 | 2003-01-21 | Akzo Nobel N.V. | Process for sulfiding a catalyst containing an S-containing additive |
FR2874838B1 (fr) * | 2004-09-08 | 2006-11-24 | Inst Francais Du Petrole | Procede de sulfuration de catalyseurs d'hydrotraitement |
US7407909B2 (en) * | 2004-10-01 | 2008-08-05 | Exxonmobil Research And Engineering Company | Ex-situ reduction and dry passivation of noble metal catalysts |
-
2003
- 2003-02-11 FR FR0301634A patent/FR2850882B1/fr not_active Expired - Lifetime
-
2004
- 2004-02-06 JP JP2006502133A patent/JP5016918B2/ja not_active Expired - Lifetime
- 2004-02-06 WO PCT/FR2004/000272 patent/WO2004071655A1/fr active Application Filing
- 2004-02-06 DE DE112004000001.7T patent/DE112004000001B4/de not_active Expired - Lifetime
- 2004-02-06 CA CA2485665A patent/CA2485665C/fr not_active Expired - Lifetime
- 2004-02-06 US US10/526,499 patent/US7582587B2/en active Active
- 2004-09-17 LU LU91102A patent/LU91102B1/fr active
Also Published As
Publication number | Publication date |
---|---|
LU91102B1 (fr) | 2006-02-28 |
FR2850882A1 (fr) | 2004-08-13 |
US7582587B2 (en) | 2009-09-01 |
JP5016918B2 (ja) | 2012-09-05 |
FR2850882B1 (fr) | 2005-03-18 |
JP2006517467A (ja) | 2006-07-27 |
WO2004071655A1 (fr) | 2004-08-26 |
US20060154812A1 (en) | 2006-07-13 |
DE112004000001T5 (de) | 2005-05-25 |
DE112004000001B4 (de) | 2021-12-02 |
CA2485665C (fr) | 2011-09-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2485665A1 (fr) | Passivation de catalyseur d'hydroconversion sulfure | |
CA2523698C (fr) | Traitement hors site de catalyseurs d'hydrogenation | |
EP1800749B1 (fr) | Procédé d'hydrogénation sélective mettant en oeuvre un catalyseur présentant un support spécifique | |
JP2006517467A5 (fr) | ||
EP1077085B1 (fr) | Précarbonation de catalyseur d'hydrotraitement | |
KR101311968B1 (ko) | 수소첨가 촉매 조성물, 그의 제조 방법 및 용도 | |
WO2022128486A1 (fr) | Procede de rejuvenation d'un catalyseur d'un procede d'hydrotraitement et/ou d'hydrocraquage | |
JP4871717B2 (ja) | 制御された多孔度を有する触媒を利用する選択的水素化法 | |
CA3119862A1 (fr) | Procede de rejuvenation d'un catalyseur d'un procede d'hydrotraitement et/ou d'hydrocraquage | |
CN1861260A (zh) | 一种硫化型加氢催化剂的制备方法 | |
CA3119861A1 (fr) | Procede de rejuvenation d'un catalyseur use non regenere d'un procede d'hydrodesulfuration d'essences | |
EP1696018B1 (fr) | Procédé de désulfuration profonde par adsorption d'une coupe hydrocarboné de type gazole | |
FR2997415A1 (fr) | Procede de production d'une essence a basse teneur en soufre | |
CA2499696C (fr) | Passivation par traitement thermique oxydant de catalyseur d'hydrotraitement sulfure | |
EP3338887A1 (fr) | Procédé de sulfuration d'un catalyseur à partir d'une coupe d'hydrocarbures préalablement hydrotraitée et d'un composé soufré | |
FR2820991A1 (fr) | Procede de sulfuration des catalyseurs d'hydrotraitement | |
FR3090006A1 (fr) | Procédé d’hydrodésulfuration de coupes essence oléfinique contenant du soufre mettant en œuvre un catalyseur réjuvéné à un composé organique. | |
WO2021224172A1 (fr) | Catalyseur d'hydrogenation comprenant un support et un ratio nimo specifique | |
EP4146384A1 (fr) | Catalyseur d'hydrogenation selective comprenant un support specifique en partie sous forme aluminate | |
RU2021136698A (ru) | Реактивированные катализаторы гидроочистки для применения в снижении выбросов серы | |
WO2023110732A1 (fr) | Procede de captation de mercaptans avec selection de temperature et rapport en ni/nio specifique | |
WO2023110733A1 (fr) | Procede de captation de mercaptans mettant en œuvre une masse de captation ayant subi une etape de passivation au co2 | |
May Lozano | Identifying the active sites in catalytic hydrodesulfuration | |
Lee et al. | Properties of sonochemically synthesized, highly dispersed MoS2/Al2O3 catalysts for the hydrodesulfurization of dibenzothiophene and 4, 6-dimethyldibenzothiophene | |
Lee et al. | The production of hydroprocessed renewable diesel with a catalyst regenerated using supercritical carbon dioxide (SCCO2) |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKEX | Expiry |
Effective date: 20240206 |