WO2002032570A3 - Hydrodemetallation catalyst and method for making same - Google Patents
Hydrodemetallation catalyst and method for making same Download PDFInfo
- Publication number
- WO2002032570A3 WO2002032570A3 PCT/US2001/032432 US0132432W WO0232570A3 WO 2002032570 A3 WO2002032570 A3 WO 2002032570A3 US 0132432 W US0132432 W US 0132432W WO 0232570 A3 WO0232570 A3 WO 0232570A3
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- catalyst
- pores
- making same
- particles
- total volume
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title abstract 6
- 238000000034 method Methods 0.000 title abstract 2
- 239000011148 porous material Substances 0.000 abstract 7
- 239000004215 Carbon black (E152) Substances 0.000 abstract 2
- 229930195733 hydrocarbon Natural products 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- 239000002184 metal Substances 0.000 abstract 2
- 229910052751 metal Inorganic materials 0.000 abstract 2
- 239000002245 particle Substances 0.000 abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract 1
- 230000002902 bimodal effect Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 150000002739 metals Chemical class 0.000 abstract 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
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/28—Molybdenum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—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
- 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
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
- B01J27/19—Molybdenum
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/635—0.5-1.0 ml/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/651—50-500 nm
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/66—Pore distribution
- B01J35/69—Pore distribution bimodal
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2002215374A AU2002215374A1 (en) | 2000-10-19 | 2001-10-16 | Hydrodemetallation catalyst and method for making same |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US69272600A | 2000-10-19 | 2000-10-19 | |
US09/692,726 | 2000-10-19 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2002032570A2 WO2002032570A2 (en) | 2002-04-25 |
WO2002032570A3 true WO2002032570A3 (en) | 2002-08-29 |
Family
ID=24781759
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2001/032432 WO2002032570A2 (en) | 2000-10-19 | 2001-10-16 | Hydrodemetallation catalyst and method for making same |
Country Status (3)
Country | Link |
---|---|
AR (1) | AR030905A1 (en) |
AU (1) | AU2002215374A1 (en) |
WO (1) | WO2002032570A2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8764972B2 (en) | 2003-12-19 | 2014-07-01 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6589908B1 (en) * | 2000-11-28 | 2003-07-08 | Shell Oil Company | Method of making alumina having bimodal pore structure, and catalysts made therefrom |
US7820036B2 (en) | 2006-08-03 | 2010-10-26 | Shell Oil Company | Highly stable heavy hydrocarbon hydrodesulfurization catalyst and methods of making and use thereof |
WO2008016971A2 (en) | 2006-08-03 | 2008-02-07 | Shell Oil Company | A catalyst containing molybdenum and a group viii metal and its use for hydrodesulfrization hydrogen distillate |
US7977274B2 (en) | 2006-09-29 | 2011-07-12 | Sd Lizenzverwertungsgesellschaft Mbh & Co. Kg | Catalyst with bimodal pore size distribution and the use thereof |
MX2007009504A (en) * | 2007-08-07 | 2009-02-06 | Mexicano Inst Petrol | Catalyst for the first stage of hydro demetallization in a hydro processing system with multiple reactors for the improvement of heavy and extra-heavy crudes. |
US8114806B2 (en) | 2008-04-10 | 2012-02-14 | Shell Oil Company | Catalysts having selected pore size distributions, method of making such catalysts, methods of producing a crude product, products obtained from such methods, and uses of products obtained |
US8734634B2 (en) | 2008-04-10 | 2014-05-27 | Shell Oil Company | Method for producing a crude product, method for preparing a diluted hydrocarbon composition, crude products, diluents and uses of such crude products and diluents |
CA2736576C (en) | 2008-09-10 | 2017-05-23 | Haldor Topsoe A/S | Hydroconversion process and catalyst |
US10603656B2 (en) | 2013-10-17 | 2020-03-31 | Shell Oil Company | Ultra-stable heavy hydrocarbon hydroprocessing catalyst and methods of making and use thereof |
CN104549329B (en) * | 2013-10-22 | 2016-08-17 | 中国石油化工股份有限公司 | The preparation method of Hydrodemetalation catalyst |
CN110773188A (en) * | 2018-07-31 | 2020-02-11 | 中国石油化工股份有限公司 | Heavy oil hydrogenation deasphaltened catalyst and preparation and application thereof |
CN110773209A (en) * | 2018-07-31 | 2020-02-11 | 中国石油化工股份有限公司 | Heavy oil hydrogenation deasphaltened catalyst and preparation and application thereof |
CN110773179A (en) * | 2018-07-31 | 2020-02-11 | 中国石油化工股份有限公司 | Alumina carrier and preparation method thereof |
CN110773183A (en) * | 2018-07-31 | 2020-02-11 | 中国石油化工股份有限公司 | Heavy oil hydrogenation deasphaltened catalyst and preparation and application thereof |
CN110773187A (en) * | 2018-07-31 | 2020-02-11 | 中国石油化工股份有限公司 | Heavy oil hydrogenation deasphaltened catalyst and preparation and application thereof |
CN110773190A (en) * | 2018-07-31 | 2020-02-11 | 中国石油化工股份有限公司 | Heavy oil hydrogenation deasphaltened catalyst and preparation and application thereof |
CN112547079A (en) * | 2019-09-25 | 2021-03-26 | 中国石油化工股份有限公司 | Heavy oil hydrotreating catalyst and application thereof |
CN116020498A (en) * | 2021-10-27 | 2023-04-28 | 中国石油化工股份有限公司 | Preparation method of hydrogenation catalyst, catalyst prepared by method and application |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4294685A (en) * | 1979-03-13 | 1981-10-13 | Electric Power Research Institute, Inc. | Process for coal liquefaction and catalyst |
US4526675A (en) * | 1983-05-26 | 1985-07-02 | Standard Oil Company (Indiana) | Hydrocarbon conversion method |
US4846961A (en) * | 1986-12-05 | 1989-07-11 | Union Oil Company Of California | Hydroprocessing catalyst with a Ni-P-Mo |
US4880525A (en) * | 1987-09-24 | 1989-11-14 | Shell Oil Company | Process for hydrotreating hydrocarbon feeds |
EP0583837A1 (en) * | 1992-08-18 | 1994-02-23 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation of a catalyst for a catalyst precursor |
-
2001
- 2001-10-16 AU AU2002215374A patent/AU2002215374A1/en not_active Abandoned
- 2001-10-16 WO PCT/US2001/032432 patent/WO2002032570A2/en active Application Filing
- 2001-10-17 AR ARP010104854A patent/AR030905A1/en unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4294685A (en) * | 1979-03-13 | 1981-10-13 | Electric Power Research Institute, Inc. | Process for coal liquefaction and catalyst |
US4526675A (en) * | 1983-05-26 | 1985-07-02 | Standard Oil Company (Indiana) | Hydrocarbon conversion method |
US4846961A (en) * | 1986-12-05 | 1989-07-11 | Union Oil Company Of California | Hydroprocessing catalyst with a Ni-P-Mo |
US4880525A (en) * | 1987-09-24 | 1989-11-14 | Shell Oil Company | Process for hydrotreating hydrocarbon feeds |
EP0583837A1 (en) * | 1992-08-18 | 1994-02-23 | Shell Internationale Researchmaatschappij B.V. | Process for the preparation of a catalyst for a catalyst precursor |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8764972B2 (en) | 2003-12-19 | 2014-07-01 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
Also Published As
Publication number | Publication date |
---|---|
AR030905A1 (en) | 2003-09-03 |
WO2002032570A2 (en) | 2002-04-25 |
AU2002215374A1 (en) | 2002-04-29 |
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