CA2357528A1 - Hydrotreating using bulk group viii/group vib catalysts - Google Patents
Hydrotreating using bulk group viii/group vib catalysts Download PDFInfo
- Publication number
- CA2357528A1 CA2357528A1 CA002357528A CA2357528A CA2357528A1 CA 2357528 A1 CA2357528 A1 CA 2357528A1 CA 002357528 A CA002357528 A CA 002357528A CA 2357528 A CA2357528 A CA 2357528A CA 2357528 A1 CA2357528 A1 CA 2357528A1
- Authority
- CA
- Canada
- Prior art keywords
- hydrotreating
- catalyst
- feedstock
- metal
- group viii
- 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
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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/16—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by oxo-reaction combined with reduction
-
- 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
- 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
-
- 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
- B01J23/88—Molybdenum
- B01J23/887—Molybdenum containing in addition other metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/8878—Chromium
-
- 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
- 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
- B01J23/8885—Tungsten containing also 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/03—Precipitation; Co-precipitation
-
- 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
- B01J37/08—Heat treatment
- B01J37/082—Decomposition and pyrolysis
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/04—Reduction, e.g. hydrogenation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/50—Partial depolymerisation
-
- 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
-
- 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
- C10G45/14—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 with moving solid particles
- C10G45/16—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 with moving solid particles suspended in the oil, e.g. slurries
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/04—Oxides
-
- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
-
- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
- C10G65/08—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a hydrogenation of the aromatic hydrocarbons
-
- 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- 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
- C10G2300/1062—Lubricating oils
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/302—Viscosity
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/44—Solvents
-
- 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
- C10G2400/10—Lubricating oil
-
- 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
- C10G2400/14—White oil, eating oil
Abstract
Hydroprocessing of petroleum and chemical feedstocks using bulk Group VIII/Group VIB catalysts. Preferred catalysts include those comprised of Ni- Mo- W.
Claims (19)
1. A process for preparing a lubricating oil basestock containing at least about 90% saturates which comprises:
(a) passing a feedstock to a hydrotreating zone containing at least one hydrotreating reactor containing a hydrotreating catalyst;
(b) hydrotreating the feedstock in the presence of the hydrotreating catalyst under hydrotreating conditions wherein the hydrotreating catalyst is a bulk metal catalyst comprising non-noble Group VIII metal molybdate in which at least a portion but less than all of molybdenum is replaced by tungsten to produce a hydrotreated feedstock; and (c) fractionating the hydrotreated feedstock.
(a) passing a feedstock to a hydrotreating zone containing at least one hydrotreating reactor containing a hydrotreating catalyst;
(b) hydrotreating the feedstock in the presence of the hydrotreating catalyst under hydrotreating conditions wherein the hydrotreating catalyst is a bulk metal catalyst comprising non-noble Group VIII metal molybdate in which at least a portion but less than all of molybdenum is replaced by tungsten to produce a hydrotreated feedstock; and (c) fractionating the hydrotreated feedstock.
2. A process for preparing a lubricating oil basestock containing at least about 90% saturates which comprises:
(a) passing a feedstock to a first hydrotreating zone containing at least one hydrotreating reactor containing a first non-bulk metal hydrotreating catalyst;
(b) hydrotreating the feedstock in the presence of the first hydrotreating catalyst under first hydrotreating conditions wherein the first hydrotreating catalyst comprises at least one Group VIB and at least one non-noble Group VIII metal on a refractory oxide support to produce a first hydrotreated feedstock;
(c) passing at least a portion of the first hydrotreated feedstock to a second hydrotreating zone containing at least one hydrotreating reactor containing a second hydrotreating catalyst;
(d) hydrotreating the first hydrotreated feedstock in the second hydrotreating zone under second hydrotreating conditions wherein the second hydrotreating catalyst in said second hydrotreating zone is a bulk metal catalyst comprising non-noble Group VIII metal molybdate in which at least a portion but less than all of molybdenum is replaced by tungsten to produce a second hydrotreated feedstock;
(e) fractionating the second hydrotreated feedstock.
(a) passing a feedstock to a first hydrotreating zone containing at least one hydrotreating reactor containing a first non-bulk metal hydrotreating catalyst;
(b) hydrotreating the feedstock in the presence of the first hydrotreating catalyst under first hydrotreating conditions wherein the first hydrotreating catalyst comprises at least one Group VIB and at least one non-noble Group VIII metal on a refractory oxide support to produce a first hydrotreated feedstock;
(c) passing at least a portion of the first hydrotreated feedstock to a second hydrotreating zone containing at least one hydrotreating reactor containing a second hydrotreating catalyst;
(d) hydrotreating the first hydrotreated feedstock in the second hydrotreating zone under second hydrotreating conditions wherein the second hydrotreating catalyst in said second hydrotreating zone is a bulk metal catalyst comprising non-noble Group VIII metal molybdate in which at least a portion but less than all of molybdenum is replaced by tungsten to produce a second hydrotreated feedstock;
(e) fractionating the second hydrotreated feedstock.
3. A process for preparing a petroleum oil containing at least about 90% saturates which comprises:
(a) passing a feedstock to a hydrotreating zone containing at least one hydrotreating reactor containing a hydrotreating catalyst;
(b) hydrotreating the feedstock in the presence of the hydrotreating catalyst under hydrotreating conditions wherein the hydrotreating catalyst is a bulk metal catalyst comprising non-noble Group VIII metal molybdate in which at least a portion but less than all of molybdenum is replaced by tungsten to produce a hydrotreated feedstock;
(c) fractionating the hydrotreated feedstock to produce a first basestock;
(d) passing the first basestock to a hydrogenation zone containing at least one hydrogenation reactor containing a hydrogenation catalyst;
(e) hydrogenating the first basestock in the presence of the hydrogenation catalyst under hydrogenation conditions wherein the hydrogenation catalyst comprises at least one Group VIII metal; and (f) fractionating the hydrogenated product from step, (e) to produce a petroleum oil containing at least about 90% saturates.
(a) passing a feedstock to a hydrotreating zone containing at least one hydrotreating reactor containing a hydrotreating catalyst;
(b) hydrotreating the feedstock in the presence of the hydrotreating catalyst under hydrotreating conditions wherein the hydrotreating catalyst is a bulk metal catalyst comprising non-noble Group VIII metal molybdate in which at least a portion but less than all of molybdenum is replaced by tungsten to produce a hydrotreated feedstock;
(c) fractionating the hydrotreated feedstock to produce a first basestock;
(d) passing the first basestock to a hydrogenation zone containing at least one hydrogenation reactor containing a hydrogenation catalyst;
(e) hydrogenating the first basestock in the presence of the hydrogenation catalyst under hydrogenation conditions wherein the hydrogenation catalyst comprises at least one Group VIII metal; and (f) fractionating the hydrogenated product from step, (e) to produce a petroleum oil containing at least about 90% saturates.
4. The process of claims 1, 2 or 3 wherein the bulk metal catalyst is represented by the formula:
(X)b(Mo)c(W)d Oz wherein X is non-noble Group VIII metal, the molar ratio of b: (c+d) is 0.5/1 to 3/1, the molar ratio of c:d is >0.01/1, and z = [2b + 6(c + d)]/2.
(X)b(Mo)c(W)d Oz wherein X is non-noble Group VIII metal, the molar ratio of b: (c+d) is 0.5/1 to 3/1, the molar ratio of c:d is >0.01/1, and z = [2b + 6(c + d)]/2.
5. The process of claim 4 wherein the molar ratio of b:(c+d) is 0.75/1 to 1.5/1.
6. The process of claim 5 wherein the molar ratio of b:(c+d) is 0.75/1 to 1.25/1.
7. The process of claim 4 wherein the molar ratio of c:d is >0.1/1.
8. The process of claim 7 wherein the molar ratio of c:d is 1/10 to 10/1.
9. The process of claim 8 wherein the molar ratio of c:d is 1/3 to 3/1.
10. The process of claim 3 wherein the hydrogenation catalyst further contains at least one Group VIB metal.
11. The process of claim 3 wherein the Group VIII metal is a non-noble metal.
12. The process of claim 11 wherein the non-noble metal is nickel.
13. The process of claims 1 or 3 wherein the hydrotreating conditions comprise temperatures of from 250 to 400 °C, hydrogen pressures of from to 3500 psig (3549 to 24234 kPa), liquid hourly space velocities of from 0.1 to 5.0 and hydrogen treat gas rates of from 500 to 5000 scf/B (89 to 890 m3/m3).
14. The process of claim 2 wherein the first hydrotreating conditions in the first hydrotreating zone comprise temperatures of from 250 to 400 °C, hydrogen pressures of from 500 to 3500 psig (3549 to 24234 kPa), liquid hourly space velocities of from 0.1 to 5.0 and hydrogen treat gas rates of from 500 to 5000 scf/B (89 to 890 m3/m3), and the second hydrotreating conditions in the second hydrotreating zone comprise temperatures of from 250 to 400 °C, hydrogen pressures of from 500 to 5000 psig (3549 to 24234 kPa), liquid hourly space velocities of from 0.1 to 5.0 and hydrogen treat gas rates of from 500 to 5000 scf/B (89 to 890 m3/m3).
15. The process of claim 3 wherein the hydrogenation conditions comprise temperatures of from 150 to 400 °C, hydrogen pressures of from to 3500 psig (3549 to 24234 kPa), liquid hourly space velocities of from 0.1 to 5.0 and hydrogen treat gas rates of from 500 to 5000 scf/B (89 to 890 m3/m3).
16. The process of claims 1, 2 or 3 wherein the petroleum oil is a white oil.
17. The process of claim 16 wherein the white oil is a technical or medicinal white oil.
18. The process of claim 4 wherein the non-noble metal is Ni or Co.
19. The process of claim 4 wherein the non-noble metal is Ni.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/231,156 | 1999-01-15 | ||
US09/231,156 US6162350A (en) | 1997-07-15 | 1999-01-15 | Hydroprocessing using bulk Group VIII/Group VIB catalysts (HEN-9901) |
PCT/US2000/001007 WO2000042131A1 (en) | 1999-01-15 | 2000-01-14 | Hydroprocessing using bulk group viii/group vib catalysts |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2357528A1 true CA2357528A1 (en) | 2000-07-20 |
CA2357528C CA2357528C (en) | 2010-08-03 |
Family
ID=22867969
Family Applications (11)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2356920A Expired - Lifetime CA2356920C (en) | 1999-01-15 | 2000-01-14 | Hydroconversion process using bulk group viii/group vib catalysts |
CA2357022A Expired - Lifetime CA2357022C (en) | 1999-01-15 | 2000-01-14 | Two stage process for hydroprocessing using bulk multimetallic catalyst |
CA002360035A Abandoned CA2360035A1 (en) | 1999-01-15 | 2000-01-14 | Improved process for preparing alcohols by the oxo process |
CA2359192A Expired - Lifetime CA2359192C (en) | 1999-01-15 | 2000-01-14 | Hydrocracking process using bulk group viii/group vib catalysts |
CA2358695A Expired - Lifetime CA2358695C (en) | 1999-01-15 | 2000-01-14 | Hydrofining process using bulk group viii/group vib catalysts |
CA2358905A Expired - Lifetime CA2358905C (en) | 1999-01-15 | 2000-01-14 | Production of low sulfur/low nitrogen hydrocrackates |
CA2357024A Expired - Lifetime CA2357024C (en) | 1999-01-15 | 2000-01-14 | Multistage hydroprocessing using bulk multimetallic catalyst |
CA2356909A Expired - Lifetime CA2356909C (en) | 1999-01-15 | 2000-01-14 | Hydroprocessing using bulk group viii/group vib catalysts |
CA2357528A Expired - Lifetime CA2357528C (en) | 1999-01-15 | 2000-01-14 | Hydrotreating using bulk group viii/group vib catalysts |
CA2358901A Expired - Lifetime CA2358901C (en) | 1999-01-15 | 2000-01-14 | Hydroprocessing using bulk multimetallic catalysts |
CA2358910A Expired - Lifetime CA2358910C (en) | 1999-01-15 | 2000-01-14 | Slurry hydroprocessing using bulk multimetallic catalysts |
Family Applications Before (8)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2356920A Expired - Lifetime CA2356920C (en) | 1999-01-15 | 2000-01-14 | Hydroconversion process using bulk group viii/group vib catalysts |
CA2357022A Expired - Lifetime CA2357022C (en) | 1999-01-15 | 2000-01-14 | Two stage process for hydroprocessing using bulk multimetallic catalyst |
CA002360035A Abandoned CA2360035A1 (en) | 1999-01-15 | 2000-01-14 | Improved process for preparing alcohols by the oxo process |
CA2359192A Expired - Lifetime CA2359192C (en) | 1999-01-15 | 2000-01-14 | Hydrocracking process using bulk group viii/group vib catalysts |
CA2358695A Expired - Lifetime CA2358695C (en) | 1999-01-15 | 2000-01-14 | Hydrofining process using bulk group viii/group vib catalysts |
CA2358905A Expired - Lifetime CA2358905C (en) | 1999-01-15 | 2000-01-14 | Production of low sulfur/low nitrogen hydrocrackates |
CA2357024A Expired - Lifetime CA2357024C (en) | 1999-01-15 | 2000-01-14 | Multistage hydroprocessing using bulk multimetallic catalyst |
CA2356909A Expired - Lifetime CA2356909C (en) | 1999-01-15 | 2000-01-14 | Hydroprocessing using bulk group viii/group vib catalysts |
Family Applications After (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2358901A Expired - Lifetime CA2358901C (en) | 1999-01-15 | 2000-01-14 | Hydroprocessing using bulk multimetallic catalysts |
CA2358910A Expired - Lifetime CA2358910C (en) | 1999-01-15 | 2000-01-14 | Slurry hydroprocessing using bulk multimetallic catalysts |
Country Status (15)
Country | Link |
---|---|
US (1) | US6162350A (en) |
EP (12) | EP1144351A1 (en) |
JP (12) | JP4766748B2 (en) |
KR (1) | KR20010101526A (en) |
CN (1) | CN1136236C (en) |
AT (7) | ATE388217T1 (en) |
AU (11) | AU757716B2 (en) |
BR (2) | BR0007821A (en) |
CA (11) | CA2356920C (en) |
DE (8) | DE60040527D1 (en) |
DK (5) | DK1169416T3 (en) |
ES (3) | ES2246828T3 (en) |
MX (1) | MXPA01007139A (en) |
NO (11) | NO20013424D0 (en) |
WO (12) | WO2000042121A1 (en) |
Families Citing this family (236)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1989008819A1 (en) * | 1988-03-15 | 1989-09-21 | Divetronic Ag | Process and device for compensating errors of measurement |
US7513989B1 (en) * | 1997-07-15 | 2009-04-07 | Exxonmobil Research And Engineering Company | Hydrocracking process using bulk group VIII/Group VIB catalysts |
US7232515B1 (en) * | 1997-07-15 | 2007-06-19 | Exxonmobil Research And Engineering Company | Hydrofining process using bulk group VIII/Group VIB catalysts |
US7229548B2 (en) * | 1997-07-15 | 2007-06-12 | Exxonmobil Research And Engineering Company | Process for upgrading naphtha |
US6620313B1 (en) * | 1997-07-15 | 2003-09-16 | Exxonmobil Research And Engineering Company | Hydroconversion process using bulk group VIII/Group VIB catalysts |
US6712955B1 (en) * | 1997-07-15 | 2004-03-30 | Exxonmobil Research And Engineering Company | Slurry hydroprocessing using bulk multimetallic catalysts |
US6758963B1 (en) * | 1997-07-15 | 2004-07-06 | Exxonmobil Research And Engineering Company | Hydroprocessing using bulk group VIII/group vib catalysts |
US6755963B2 (en) * | 1997-07-15 | 2004-06-29 | Exxonmobil Chemical Patents Inc. | Hydrogenation process for hydrocarbon resins |
US6582590B1 (en) * | 1997-07-15 | 2003-06-24 | Exxonmobil Research And Engineering Company | Multistage hydroprocessing using bulk multimetallic catalyst |
US7288182B1 (en) * | 1997-07-15 | 2007-10-30 | Exxonmobil Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts |
US6863803B1 (en) * | 1997-07-15 | 2005-03-08 | Exxonmobil Research And Engineering Company | Production of low sulfur/low nitrogen hydrocrackates |
US6783663B1 (en) * | 1997-07-15 | 2004-08-31 | Exxonmobil Research And Engineering Company | Hydrotreating using bulk multimetallic catalysts |
US6162350A (en) * | 1997-07-15 | 2000-12-19 | Exxon Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts (HEN-9901) |
US6534437B2 (en) | 1999-01-15 | 2003-03-18 | Akzo Nobel N.V. | Process for preparing a mixed metal catalyst composition |
US6281158B1 (en) * | 1999-02-15 | 2001-08-28 | Shell Oil Company | Preparation of a co-containing hydrotreating catalyst precursor and catalyst |
WO2000048971A1 (en) * | 1999-02-22 | 2000-08-24 | Symyx Technologies, Inc. | Compositions comprising nickel and their use as catalyst in oxidative dehydrogenation of alkanes |
US6841512B1 (en) * | 1999-04-12 | 2005-01-11 | Ovonic Battery Company, Inc. | Finely divided metal catalyst and method for making same |
US6372125B1 (en) * | 1999-08-23 | 2002-04-16 | Institut Francais Du Petrole | Catalyst comprising a group VIB metal carbide, phosphorous and its use for hydrodesulphurisation and hydrogenation of gas oils |
DE60134140D1 (en) * | 2000-07-12 | 2008-07-03 | Albemarle Netherlands Bv | METHOD FOR PRODUCING AN ADDITIVELY CONTAINING MIXED METAL CATALYST |
ES2362349T3 (en) * | 2000-07-12 | 2011-07-01 | Albemarle Netherlands B.V. | MIXED METAL CATALYST THAT INCLUDES A COMBUSTIBLE BINDER. |
US6632414B2 (en) * | 2001-03-30 | 2003-10-14 | Corning Incorporated | Mini-structured catalyst beds for three-phase chemical processing |
US6515033B2 (en) | 2001-05-11 | 2003-02-04 | Chevron U.S.A. Inc. | Methods for optimizing fischer-tropsch synthesis hydrocarbons in the distillate fuel range |
US6515034B2 (en) | 2001-05-11 | 2003-02-04 | Chevron U.S.A. Inc. | Co-hydroprocessing of Fischer-Tropsch products and crude oil fractions |
FR2838743A1 (en) * | 2002-04-18 | 2003-10-24 | Centre Nat Rech Scient | Conversion of branched (co)polymers into other (co)polymers, e.g. waste polypropylene into usable polyethylene, by metal hydride or organometallic complex-catalyzed cleavage of branches |
ATE370917T1 (en) * | 2002-06-25 | 2007-09-15 | Albemarle Netherlands Bv | USE OF CATIONIC LAYER MATERIALS, COMPOSITIONS OF THESE MATERIALS AND THE PRODUCTION OF CATIONIC LAYER MATERIALS |
FR2842202A1 (en) * | 2002-07-11 | 2004-01-16 | Bp Lavera Snc | STYRENE TERPOLYMER AND METHOD FOR THE CONTROLLED TRANSFORMATION OF HYDROCARBON POLYMERS |
US7173160B2 (en) | 2002-07-18 | 2007-02-06 | Chevron U.S.A. Inc. | Processes for concentrating higher diamondoids |
FR2843050B1 (en) * | 2002-08-01 | 2005-04-15 | Inst Francais Du Petrole | METAL CATALYST OF GROUP VI AND GROUP VIII AT LEAST IN PART IN THE FORM OF HETEROPOLYANIONS IN THE OXIDE PRECURSOR |
AR043242A1 (en) * | 2003-02-24 | 2005-07-20 | Shell Int Research | PREPARATION AND USE OF A CATALYST COMPOSITION |
AR043243A1 (en) * | 2003-02-24 | 2005-07-20 | Shell Int Research | CATALYST COMPOSITION, ITS PREPARATION AND USE |
US7598202B2 (en) * | 2003-06-24 | 2009-10-06 | Albemarle Netherlands B.V. | Use of cationic layered materials, compositions comprising these materials, and the preparation of cationic layered materials |
US6951830B2 (en) * | 2003-08-05 | 2005-10-04 | Exxonmobil Chemical Patents Inc. | Molecular sieve catalyst compositions, their production and use in conversion processes |
CA2540517A1 (en) * | 2003-10-02 | 2006-03-28 | Exxonmobil Research And Engineering Company | Process for upgrading naphtha |
US7816299B2 (en) * | 2003-11-10 | 2010-10-19 | Exxonmobil Research And Engineering Company | Hydrotreating catalyst system suitable for use in hydrotreating hydrocarbonaceous feedstreams |
AU2004288905A1 (en) * | 2003-11-10 | 2005-05-26 | Exxonmobil Research And Engineering Company | A hydrotreating catalyst system suitable for use in hydrotreating hydrocarbonaceous feedstreams |
US20050109679A1 (en) * | 2003-11-10 | 2005-05-26 | Schleicher Gary P. | Process for making lube oil basestocks |
US7597795B2 (en) * | 2003-11-10 | 2009-10-06 | Exxonmobil Research And Engineering Company | Process for making lube oil basestocks |
US7745369B2 (en) | 2003-12-19 | 2010-06-29 | Shell Oil Company | Method and catalyst for producing a crude product with minimal hydrogen uptake |
US20100098602A1 (en) | 2003-12-19 | 2010-04-22 | Opinder Kishan Bhan | Systems, methods, and catalysts for producing a crude product |
CN1894374A (en) * | 2003-12-19 | 2007-01-10 | 国际壳牌研究有限公司 | Systems, methods, and catalysts for producing a crude product |
US7628908B2 (en) | 2003-12-19 | 2009-12-08 | Shell Oil Company | Systems, methods, and catalysts for producing a crude product |
US7879223B2 (en) | 2003-12-19 | 2011-02-01 | Shell Oil Company | Systems and methods of producing a crude product |
NL1027761C2 (en) * | 2003-12-19 | 2006-09-20 | Shell Int Research | Systems, methods and catalysts for producing a crude product. |
CA2455011C (en) | 2004-01-09 | 2011-04-05 | Suncor Energy Inc. | Bituminous froth inline steam injection processing |
CA2455149C (en) * | 2004-01-22 | 2006-04-11 | Suncor Energy Inc. | In-line hydrotreatment process for low tan synthetic crude oil production from oil sand |
US7776205B2 (en) * | 2004-04-22 | 2010-08-17 | Exxonmobil Research And Engineering Company | Process to upgrade hydrocarbonaceous feedstreams |
US7691257B2 (en) * | 2004-04-22 | 2010-04-06 | Exxonmobil Research And Engineering Company | Process to manufacture low sulfur diesel fuels |
US7780845B2 (en) * | 2004-04-22 | 2010-08-24 | Exxonmobil Research And Engineering Company | Process to manufacture low sulfur distillates |
EP1763572A2 (en) * | 2004-06-22 | 2007-03-21 | Albemarle Netherlands B.V. | Process for upgrading liquid hydrocarbon feeds |
US7629289B2 (en) * | 2004-06-23 | 2009-12-08 | Uop Llc | Selective naphtha desulfurization process and catalyst |
EP1794264B1 (en) * | 2004-09-08 | 2020-05-27 | Shell International Research Maatschappij B.V. | Hydrocracking catalyst composition |
US7737072B2 (en) * | 2004-09-10 | 2010-06-15 | Chevron Usa Inc. | Hydroprocessing bulk catalyst and uses thereof |
US7972499B2 (en) | 2004-09-10 | 2011-07-05 | Chevron U.S.A. Inc. | Process for recycling an active slurry catalyst composition in heavy oil upgrading |
US7678732B2 (en) | 2004-09-10 | 2010-03-16 | Chevron Usa Inc. | Highly active slurry catalyst composition |
EP1791639A1 (en) * | 2004-09-22 | 2007-06-06 | Exxonmobil Research And Engineering Company | BULK Ni-Mo-W CATALYSTS MADE FROM PRECURSORS CONTAINING AN ORGANIC AGENT |
WO2006099716A1 (en) * | 2005-03-24 | 2006-09-28 | University Of Regina | Catalysts for hydrogen production |
EP1874897A1 (en) * | 2005-04-11 | 2008-01-09 | Shell Internationale Research Maatschappij B.V. | Method and catalyst for producing a crude product having a reduced mcr content |
CA2604011A1 (en) * | 2005-04-11 | 2006-10-19 | Shell Internationale Research Maatschappij B.V. | Systems, methods, and catalysts for producing a crude product |
BRPI0609416A2 (en) | 2005-04-11 | 2011-10-11 | Shell Int Research | method to produce a gross product |
KR101281134B1 (en) * | 2005-04-21 | 2013-07-02 | 리서치 인스티튜트 오브 페트롤리움 프로세싱 시노펙 | A hydrogenation catalyst and its application |
MXPA05009283A (en) * | 2005-08-31 | 2007-02-27 | Mexicano Inst Petrol | Method of preparing a catalytic composition for the hydroprocessing of petroleum fractions. |
CA2626139C (en) * | 2005-10-26 | 2012-07-03 | Exxonmobil Research And Engineering Company | Hydroprocessing using hydrothermally-prepared bulk multimetallic catalysts |
EP1951427B1 (en) * | 2005-10-26 | 2019-09-18 | Albemarle Netherlands BV | A bulk catalyst comprising nickel tungsten metal oxidic particles and a method of preparation thereof |
AU2006308080B2 (en) * | 2005-10-26 | 2012-05-03 | Albemarle Netherlands B.V. | A bulk catalyst composition and a process preparing the bulk catalyst composition |
CA2630365C (en) | 2005-11-23 | 2010-03-16 | Pedro Pereira-Almao | Ultradispersed catalyst compositions and methods of preparation |
US7431822B2 (en) | 2005-12-16 | 2008-10-07 | Chevron U.S.A. Inc. | Process for upgrading heavy oil using a reactor with a novel reactor separation system |
US8048292B2 (en) * | 2005-12-16 | 2011-11-01 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US7938954B2 (en) | 2005-12-16 | 2011-05-10 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US8435400B2 (en) | 2005-12-16 | 2013-05-07 | Chevron U.S.A. | Systems and methods for producing a crude product |
US7943036B2 (en) * | 2009-07-21 | 2011-05-17 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US7931796B2 (en) | 2008-09-18 | 2011-04-26 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US8372266B2 (en) | 2005-12-16 | 2013-02-12 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US7713407B2 (en) | 2006-06-02 | 2010-05-11 | Exxonmobil Research & Engineering Company | Production of low sulfur fuels using improved hydrocracker post-treatment catalyst |
EP2049250A2 (en) * | 2006-07-06 | 2009-04-22 | W.R. Grace & CO. - CONN. | Aluminum sulfate bound catalysts |
TWI311498B (en) * | 2006-07-19 | 2009-07-01 | Lg Chemical Ltd | Catalyst for partial oxidation of methylbenzenes, method for preparing the same, and method for producing aromatic aldehydes using the same |
US20080087578A1 (en) | 2006-10-06 | 2008-04-17 | Bhan Opinder K | Methods for producing a crude product and compositions thereof |
US7951746B2 (en) | 2006-10-11 | 2011-05-31 | Exxonmobil Research And Engineering Company | Bulk group VIII/group VIB metal catalysts and method of preparing same |
AU2007308132B2 (en) | 2006-10-11 | 2011-12-15 | Exxonmobil Research And Engineering Company | Hydroprocessing methods for bulk group VIII/VIB metal catalysts |
US20080139380A1 (en) * | 2006-12-06 | 2008-06-12 | Chevron U.S.A. Inc. | Concentration of active catalyst slurry |
EP2102315B1 (en) * | 2006-12-19 | 2017-08-02 | ExxonMobil Research and Engineering Company | Method to prepare high activity supported distillate hydroprocessing catalysts |
US8013195B2 (en) * | 2007-06-15 | 2011-09-06 | Uop Llc | Enhancing conversion of lignocellulosic biomass |
US8158842B2 (en) * | 2007-06-15 | 2012-04-17 | Uop Llc | Production of chemicals from pyrolysis oil |
US7960520B2 (en) | 2007-06-15 | 2011-06-14 | Uop Llc | Conversion of lignocellulosic biomass to chemicals and fuels |
US7838696B2 (en) * | 2007-10-31 | 2010-11-23 | Chevron U. S. A. Inc. | Hydroconversion process employing multi-metallic catalysts and method for making thereof |
MX2010004665A (en) * | 2007-10-31 | 2010-08-04 | Chevron Usa Inc | Hydroprocessing bulk catalyst and uses thereof. |
US20090107880A1 (en) * | 2007-10-31 | 2009-04-30 | Chevron U.S.A. Inc. | Method of upgrading heavy hydrocarbon streams to jet products |
CA2705156C (en) | 2007-11-09 | 2016-01-19 | Exxonmobil Research And Engineering Company | Preparation of bulk metallic group viii/group vib metal catalysts |
BRPI0819624B1 (en) * | 2007-11-19 | 2017-12-12 | Shell Internationale Research Maatschappij B.V. | METHOD FOR DETERMINING A HYDROTRATING PROCESS USING A METALLIC BATTERY CATALYST |
CN101932381B (en) * | 2007-12-04 | 2014-04-30 | 埃克森美孚研究工程公司 | Hydrocarbon hydroprocessing using bulk catalyst composition |
US7594991B2 (en) | 2007-12-28 | 2009-09-29 | Exxonmobil Research And Engineering Company | All catalytic medicinal white oil production |
FR2927267B1 (en) * | 2008-02-07 | 2010-04-16 | Inst Francais Du Petrole | SELECTIVE HYDROGENATION CATALYST AND PROCESS FOR PREPARING THE SAME |
CN101544904B (en) * | 2008-03-28 | 2012-11-14 | 中国科学院大连化学物理研究所 | Composite metal oxide catalyst, preparation and application thereof |
WO2009134941A2 (en) * | 2008-04-29 | 2009-11-05 | Iovation Inc. | System and method for facilitating secure payment in digital transactions |
US20090023965A1 (en) | 2008-05-01 | 2009-01-22 | Intevep, S.A. | Dispersed metal sulfide-based catalysts |
US7931797B2 (en) * | 2009-07-21 | 2011-04-26 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US7897036B2 (en) | 2008-09-18 | 2011-03-01 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US7935243B2 (en) | 2008-09-18 | 2011-05-03 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US20110017637A1 (en) * | 2009-07-21 | 2011-01-27 | Bruce Reynolds | Systems and Methods for Producing a Crude Product |
US7897035B2 (en) | 2008-09-18 | 2011-03-01 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
US8236169B2 (en) | 2009-07-21 | 2012-08-07 | Chevron U.S.A. Inc | Systems and methods for producing a crude product |
FR2940313B1 (en) * | 2008-12-18 | 2011-10-28 | Inst Francais Du Petrole | HYDROCRACKING PROCESS INCLUDING PERMUTABLE REACTORS WITH LOADS CONTAINING 200PPM WEIGHT-2% WEIGHT OF ASPHALTENES |
FR2940143B1 (en) * | 2008-12-18 | 2015-12-11 | Inst Francais Du Petrole | HYDRODEMETALLATION AND HYDRODESULFURIZATION CATALYSTS AND IMPLEMENTATION IN A SINGLE FORMULATION CHAINING PROCESS |
US7964524B2 (en) * | 2009-04-29 | 2011-06-21 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
US7964526B2 (en) * | 2009-04-29 | 2011-06-21 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
EA020199B1 (en) * | 2009-04-29 | 2014-09-30 | Шеврон Ю.Эс.Эй. Инк. | Hydroconversion multi-metallic catalyst and method for making same |
US8383543B2 (en) * | 2009-04-29 | 2013-02-26 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
US7964525B2 (en) * | 2009-04-29 | 2011-06-21 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
US8058203B2 (en) * | 2009-04-29 | 2011-11-15 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
US7931799B2 (en) * | 2009-04-29 | 2011-04-26 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
US8080492B2 (en) * | 2009-04-29 | 2011-12-20 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
US8686203B2 (en) | 2009-06-12 | 2014-04-01 | Exxonmobil Research And Engineering Company | Process for preparing diesel fuels using vegetable oils or fatty acid derivatives |
US8734638B2 (en) | 2009-06-19 | 2014-05-27 | Exxonmobil Research And Engineering Company | Ebullating bed methods for treatment of biocomponent feedstocks |
CN102471698A (en) * | 2009-07-17 | 2012-05-23 | 埃克森美孚研究工程公司 | Hydroprocessing of biocomponent feedstocks with FCC off-gas |
US8927448B2 (en) | 2009-07-21 | 2015-01-06 | Chevron U.S.A. Inc. | Hydroprocessing catalysts and methods for making thereof |
US8759242B2 (en) | 2009-07-21 | 2014-06-24 | Chevron U.S.A. Inc. | Hydroprocessing catalysts and methods for making thereof |
US9068132B2 (en) | 2009-07-21 | 2015-06-30 | Chevron U.S.A. Inc. | Hydroprocessing catalysts and methods for making thereof |
US8816141B2 (en) * | 2009-08-28 | 2014-08-26 | Exxonmobil Research And Engineering Company | Reducing hydrogen consumption in hydrotreating of biocomponent feeds |
AU2010292468A1 (en) * | 2009-09-08 | 2012-04-19 | Exxonmobil Research And Engineering Company | Fuel production from feedstock containing lipidic material |
CN102510893A (en) * | 2009-09-25 | 2012-06-20 | 埃克森美孚研究工程公司 | Fuel production from feedstock containing triglyceride and/or fatty acid alkyl ester |
IT1398288B1 (en) * | 2009-09-30 | 2013-02-22 | Eni Spa | TRANSITIONAL METAL-MIXED OXIDES, TREATMENT CATALYSTS OBTAINED BY THEM, AND PREPARATION PROCESS INCLUDING SOL-GEL PROCEDURES |
CN102639678A (en) * | 2009-10-05 | 2012-08-15 | 埃克森美孚研究工程公司 | Stacking of low activity or regenerated catalyst above higher activity catalyst |
US8212099B2 (en) * | 2009-11-05 | 2012-07-03 | Chevron U.S.A. Inc. | N-paraffin selective hydroconversion process using borosilicate ZSM-48 molecular sieves |
US8604254B2 (en) | 2009-11-11 | 2013-12-10 | Dow Global Technologies Llc | Reductive hydroformylation of an alkylene to an alkanol |
CN102906231B (en) | 2009-12-08 | 2015-11-25 | 埃克森美孚研究工程公司 | Use the method for body catalyst hydrotreatment height nitrogen charging |
CN102781575B (en) * | 2009-12-18 | 2015-07-22 | 埃克森美孚研究工程公司 | Hydroprocessing catalysts and their production |
US8853474B2 (en) * | 2009-12-29 | 2014-10-07 | Exxonmobil Research And Engineering Company | Hydroprocessing of biocomponent feedstocks with low purity hydrogen-containing streams |
WO2011115695A1 (en) * | 2010-03-15 | 2011-09-22 | Exxonmobil Chemical Patents Inc. | Processes for the production of alcohols |
US20120016167A1 (en) | 2010-07-15 | 2012-01-19 | Exxonmobil Research And Engineering Company | Hydroprocessing of biocomponent feeds with low pressure hydrogen-containing streams |
US8557106B2 (en) | 2010-09-30 | 2013-10-15 | Exxonmobil Research And Engineering Company | Hydrocracking process selective for improved distillate and improved lube yield and properties |
US10144882B2 (en) | 2010-10-28 | 2018-12-04 | E I Du Pont De Nemours And Company | Hydroprocessing of heavy hydrocarbon feeds in liquid-full reactors |
CN107460001B (en) | 2010-11-04 | 2020-04-28 | 雅宝欧洲有限责任公司 | Hydrodeoxygenation of pyrolysis oils in the presence of mixed alcohols |
US20120172205A1 (en) | 2010-12-30 | 2012-07-05 | Chevron Corporation | Hydroprocessing catalysts and methods for making thereof |
US9109176B2 (en) | 2011-03-28 | 2015-08-18 | Exxonmobil Research And Engineering Company | Method for making marine bunker fuels |
ITMI20110510A1 (en) * | 2011-03-30 | 2012-10-01 | Eni Spa | TRANSITIONAL METAL MIXED OXIDES, TREATMENT CATALYSTS OBTAINED BY THEM, AND PREPARATION PROCESS |
WO2012156294A1 (en) * | 2011-05-13 | 2012-11-22 | Shell Internationale Research Maatschappij B.V. | Hydrotreating catalyst comprising a group viii and/or group vib metal silicide compound |
WO2012170520A1 (en) | 2011-06-09 | 2012-12-13 | Micromidas Inc. | Utilizing a multiphase reactor for the conversion of biomass to produce substituted furans |
US8222464B2 (en) | 2011-07-28 | 2012-07-17 | Uop Llc | Catalytic process for continuously generating polyols |
US8222465B2 (en) | 2011-07-28 | 2012-07-17 | Uop Llc | Catalytic process for continuously generating polyols |
US8323937B2 (en) | 2011-07-28 | 2012-12-04 | Uop Llc | Continuous catalytic generation of polyols from cellulose |
US8410319B2 (en) | 2011-07-28 | 2013-04-02 | Uop Llc | Continuous catalytic generation of polyols from cellulose with recycle |
US8222463B2 (en) | 2011-07-28 | 2012-07-17 | Uop Llc | Process for generation of polyols from saccharide containing feedstock |
US8222462B2 (en) | 2011-07-28 | 2012-07-17 | Uop Llc | Process for generation of polyols from saccharides |
RU2468864C1 (en) * | 2011-10-25 | 2012-12-10 | Российская Федерация, От Имени Которой Выступает Министерство Промышленности И Торговли Российской Федерации | Catalyst, method of its preparation and method of hydrorefining diesel distillates |
US20130150641A1 (en) * | 2011-12-09 | 2013-06-13 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US8704007B2 (en) | 2011-12-09 | 2014-04-22 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US9199909B2 (en) * | 2011-12-09 | 2015-12-01 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US9035115B2 (en) * | 2011-12-09 | 2015-05-19 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US8884077B2 (en) | 2011-12-09 | 2014-11-11 | Chevron U.S.A. Inc. | Hydroconversion of renewable feedstocks |
US9327275B2 (en) | 2012-09-05 | 2016-05-03 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalysts and method for making thereof |
TW201431844A (en) | 2012-10-26 | 2014-08-16 | Micromidas Inc | Methods for producing 5-(halomethyl)furfural |
US9321037B2 (en) | 2012-12-14 | 2016-04-26 | Chevron U.S.A., Inc. | Hydroprocessing co-catalyst compositions and methods of introduction thereof into hydroprocessing units |
US9687823B2 (en) | 2012-12-14 | 2017-06-27 | Chevron U.S.A. Inc. | Hydroprocessing co-catalyst compositions and methods of introduction thereof into hydroprocessing units |
KR102267501B1 (en) * | 2013-01-08 | 2021-06-21 | 사우디 아라비안 오일 컴퍼니 | Method for optimizing catalyst loading for hydrocracking process |
US20140206915A1 (en) | 2013-01-18 | 2014-07-24 | Chevron U.S.A. Inc. | Paraffinic jet and diesel fuels and base oils from vegetable oils via a combination of hydrotreating, paraffin disproportionation and hydroisomerization |
EP2970167A4 (en) * | 2013-03-14 | 2016-11-16 | Micromidas Inc | Solid forms of 5-(halomethyl) furfural and methods for preparing thereof |
MX2015012878A (en) | 2013-03-14 | 2016-02-03 | Micromidas Inc | Methods for purifying 5-(halomethyl)furfural. |
US9650312B2 (en) | 2013-03-14 | 2017-05-16 | Lummus Technology Inc. | Integration of residue hydrocracking and hydrotreating |
AR096953A1 (en) * | 2013-07-17 | 2016-02-10 | Basf Corp | PROCESS AND CATALYST FOR RESIN HYDROGENATION |
CN111662253A (en) | 2013-09-20 | 2020-09-15 | 微麦德斯公司 | Process for producing 5- (halomethyl) furfural |
KR102278425B1 (en) * | 2013-11-15 | 2021-07-19 | 셰브런 유.에스.에이.인크. | Lubricating base oil production |
RU2544996C1 (en) * | 2013-11-27 | 2015-03-20 | Общество с ограниченной ответственностью "ЛУКОЙЛ-Нижегороднефтеоргсинтез" (ООО "ЛУКОЙЛ-Нижегороднефтеоргсинтез") | Method of producing high-viscosity index base oils |
US10273420B2 (en) | 2014-10-27 | 2019-04-30 | Uop Llc | Process for hydrotreating a hydrocarbons stream |
CN104530317B (en) * | 2014-11-27 | 2017-12-29 | 宁波职业技术学院 | A kind of preparation method for being hydrogenated with indene resin |
KR20170092620A (en) | 2014-12-04 | 2017-08-11 | 엑손모빌 리서치 앤드 엔지니어링 컴퍼니 | Low sulfur marine bunker fuels and methods of making same |
CN104693359B (en) * | 2015-02-15 | 2017-08-29 | 广西大学 | Trans-critical cycle reaction system hydrogenation modification rosin and C9/C5 Petropols method and devices |
CN104815697A (en) * | 2015-05-20 | 2015-08-05 | 南开大学 | Preparation method for preparing biological aviation kerosene ultra-dispersed hydrodeoxygenation and hydroisomerization catalysts from castor oil |
US10052614B2 (en) | 2015-12-15 | 2018-08-21 | Uop Llc | Mixed metal oxides |
US10233398B2 (en) | 2015-12-15 | 2019-03-19 | Uop Llc | Crystalline transition metal oxy-hydroxide molybdotungstate |
US10400181B2 (en) | 2015-12-15 | 2019-09-03 | Uop Llc | Crystalline bis-ammonia metal molybdate |
US10322404B2 (en) | 2015-12-15 | 2019-06-18 | Uop Llc | Crystalline transition metal oxy-hydroxide molybdate |
US10005812B2 (en) | 2015-12-15 | 2018-06-26 | Uop Llc | Transition metal molybdotungsten oxy-hydroxide |
US10053637B2 (en) | 2015-12-15 | 2018-08-21 | Uop Llc | Transition metal tungsten oxy-hydroxide |
US10449523B2 (en) | 2015-12-15 | 2019-10-22 | Uop Llc | Crystalline bis-ammonia transition metal molybdotungstate |
US10046315B2 (en) | 2015-12-15 | 2018-08-14 | Uop Llc | Crystalline transition metal molybdotungstate |
US10399065B2 (en) | 2015-12-15 | 2019-09-03 | Uop Llc | Crystalline transition metal tungstate |
US10052616B2 (en) | 2015-12-15 | 2018-08-21 | Uop Llc | Crystalline ammonia transition metal molybdotungstate |
US10232357B2 (en) | 2015-12-15 | 2019-03-19 | Uop Llc | Crystalline ammonia transition metal molybdate |
US10399063B2 (en) | 2015-12-15 | 2019-09-03 | Uop Llc | Mixed metal oxides |
CN106994350B (en) * | 2016-01-22 | 2019-12-20 | 中国科学院大连化学物理研究所 | Gasoline selective hydrodesulfurization bulk phase catalyst and preparation and application thereof |
US10414995B2 (en) | 2016-03-31 | 2019-09-17 | Exxonmobil Research And Engineering Company | Base stocks and lubricant compositions containing same |
EP3458552A1 (en) | 2016-05-17 | 2019-03-27 | Exxonmobil Research And Engineering Company | Jet and diesel selective hydrocracking |
EP3526312A1 (en) | 2016-10-14 | 2019-08-21 | ExxonMobil Research and Engineering Company | Lubricant basestock production with enhanced aromatic saturation |
CA3042972C (en) * | 2016-11-07 | 2024-02-20 | Hindustan Petroleum Corporation Limited | Process for producing lighter distillates |
CN106693997B (en) * | 2017-01-10 | 2019-05-31 | 中国石油大学(华东) | A kind of diesel hydrogenation for removal sulphur catalyst and its preparation method and application |
US11788017B2 (en) | 2017-02-12 | 2023-10-17 | Magëmã Technology LLC | Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil |
US10655074B2 (en) | 2017-02-12 | 2020-05-19 | Mag{hacek over (e)}m{hacek over (a)} Technology LLC | Multi-stage process and device for reducing environmental contaminates in heavy marine fuel oil |
US10604709B2 (en) | 2017-02-12 | 2020-03-31 | Magēmā Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials |
US20190040326A1 (en) | 2017-08-03 | 2019-02-07 | Exxonmobil Research And Engineering Company | Blocked operation for group ii and group iii lubricant production |
CN110997144A (en) | 2017-08-03 | 2020-04-10 | 埃克森美孚研究工程公司 | Activation of noble metal catalysts on siliceous supports using aqueous gas streams |
RU2665484C1 (en) * | 2017-08-25 | 2018-08-30 | Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) | Method for producing catalyst and method for hydrogening oil-polymeric resins at its presence |
US10882030B2 (en) | 2017-08-25 | 2021-01-05 | Uop Llc | Crystalline transition metal tungstate |
US10773245B2 (en) | 2017-08-25 | 2020-09-15 | Uop Llc | Crystalline transition metal molybdotungstate |
US10875013B2 (en) | 2017-12-20 | 2020-12-29 | Uop Llc | Crystalline oxy-hydroxide transition metal molybdotungstate |
US11117811B2 (en) | 2017-12-20 | 2021-09-14 | Uop Llc | Highly active quaternary metallic materials using short-chain alkyl quaternary ammonium compounds |
US11078088B2 (en) | 2017-12-20 | 2021-08-03 | Uop Llc | Highly active multimetallic materials using short-chain alkyl quaternary ammonium compounds |
US10843176B2 (en) * | 2017-12-20 | 2020-11-24 | Uop Llc | Highly active quaternary metallic materials using short-chain alkyl quaternary ammonium compounds |
US10995013B2 (en) | 2017-12-20 | 2021-05-04 | Uop Llc | Mixed transition metal tungstate |
US10822247B2 (en) | 2017-12-20 | 2020-11-03 | Uop Llc | Highly active trimetallic materials using short-chain alkyl quaternary ammonium compounds |
US11034591B2 (en) | 2017-12-20 | 2021-06-15 | Uop Llc | Highly active quaternary metallic materials using short-chain alkyl quaternary ammonium compounds |
US11007515B2 (en) | 2017-12-20 | 2021-05-18 | Uop Llc | Highly active trimetallic materials using short-chain alkyl quaternary ammonium compounds |
TW201932583A (en) | 2017-12-21 | 2019-08-16 | 美商艾克頌美孚研究工程公司 | Group III base stocks and lubricant compositions |
TW201934734A (en) | 2017-12-21 | 2019-09-01 | 美商艾克頌美孚研究工程公司 | Lubricant compositions having improved oxidation performance |
TW201934731A (en) | 2017-12-21 | 2019-09-01 | 美商艾克頌美孚研究工程公司 | Group III base stocks and lubricant compositions |
TW201930575A (en) | 2017-12-21 | 2019-08-01 | 美商艾克頌美孚研究工程公司 | Lubricant compositions having improved low temperature performance |
US10808189B2 (en) | 2018-05-07 | 2020-10-20 | Exxonmobil Research And Engineering Company | Process for production of base stocks |
US11033883B2 (en) | 2018-06-26 | 2021-06-15 | Uop Llc | Transition metal molybdotungstate material |
US10688479B2 (en) | 2018-06-26 | 2020-06-23 | Uop Llc | Crystalline transition metal tungstate |
US10682632B2 (en) | 2018-06-26 | 2020-06-16 | Uop Llc | Transition metal tungstate material |
US10737248B2 (en) | 2018-06-26 | 2020-08-11 | Uop Llc | Crystalline transition metal tungstate |
US10737249B2 (en) | 2018-06-26 | 2020-08-11 | Uop Llc | Crystalline transition metal molybdotungstate |
EP3814456A1 (en) | 2018-06-26 | 2021-05-05 | ExxonMobil Research and Engineering Company | Production of improved base stocks |
US10737246B2 (en) | 2018-06-29 | 2020-08-11 | Uop Llc | Poorly crystalline transition metal tungstate |
US10981151B2 (en) | 2018-06-29 | 2021-04-20 | Uop Llc | Poorly crystalline transition metal molybdotungstate |
RU2675361C1 (en) * | 2018-08-06 | 2018-12-19 | Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) | Method for producing catalyst and method for hydrogenating oil-polymeric resins at its presence |
US10933407B2 (en) | 2018-12-13 | 2021-03-02 | Uop Llc | Ammonia-free synthesis for Al or Si based multimetallic materials |
US11213803B2 (en) | 2018-12-13 | 2022-01-04 | Uop Llc | Ammonia-free synthesis for Al or Si based multimetallic materials |
US20200270533A1 (en) * | 2019-02-22 | 2020-08-27 | Exxonmobil Research And Engineering Company | Hydroprocessing feedstocks having silicon content |
US11426711B2 (en) | 2019-05-22 | 2022-08-30 | Uop Llc | Method of making highly active metal oxide and metal sulfide materials |
WO2021028839A1 (en) | 2019-08-12 | 2021-02-18 | Chevron U.S.A. Inc. | Process for improving base oil yields |
JP2022551943A (en) | 2019-10-11 | 2022-12-14 | ヴェクター ヴィターレ アイピー エルエルシー | Rubidium and/or zinc compounds for treating Parkinson's disease and other neurodegenerative diseases |
US11185850B2 (en) | 2019-12-02 | 2021-11-30 | Saudi Arabian Oil Company | Dual functional composite catalyst for olefin metathesis and cracking |
CN110961127A (en) * | 2019-12-09 | 2020-04-07 | 大连理工大学 | Method for preparing loaded DCPD resin hydrogenation catalyst by using hydrotalcite-like compound as precursor |
CN111333752B (en) * | 2020-02-28 | 2021-06-08 | 宁波工程学院 | Hydrogenation catalysis method of carbon nine resin |
FR3111827B1 (en) | 2020-06-29 | 2022-08-19 | Ifp Energies Now | TRIMETALLIC CATALYST BASED ON NICKEL, MOLYBDENUM AND TUNGSTEN AND ITS USE IN A HYDROTREATING AND/OR HYDROCRACKING PROCESS |
US11826738B2 (en) | 2020-07-27 | 2023-11-28 | Uop Llc | High activity and high distillate yield hydrocracking catalysts with intimate interaction between unsupported metal oxide and zeolite |
KR20230045596A (en) | 2020-08-07 | 2023-04-04 | 토탈에너지스 원테크 | How to make white oil |
KR20230048306A (en) | 2020-08-07 | 2023-04-11 | 토탈에너지스 원테크 | How to make white oil |
CN111825846B (en) * | 2020-08-12 | 2021-10-22 | 广西壮族自治区林业科学研究院 | Light-colored high-stability water-soluble rosin resin and preparation method thereof |
US20230398528A1 (en) * | 2020-08-19 | 2023-12-14 | ExxonMobil Technology and Engineering Company | Tungsten-containing bulk catalysts, method of making the same, and their use in low pressure diesel hydroprocessing |
WO2022164861A1 (en) | 2021-01-26 | 2022-08-04 | Chevron U.S.A. Inc. | Process for making bright stock base oil products |
CN116888244A (en) | 2021-01-26 | 2023-10-13 | 雪佛龙美国公司 | Process for manufacturing heavy grade base oil products |
US11384297B1 (en) * | 2021-02-04 | 2022-07-12 | Saudi Arabian Oil Company | Systems and methods for upgrading pyrolysis oil to light aromatics over mixed metal oxide catalysts |
WO2023015168A1 (en) | 2021-08-06 | 2023-02-09 | ExxonMobil Technology and Engineering Company | Hydro-dealkylation process to generate high quality fuels, base stocks and waxes |
WO2023114839A1 (en) | 2021-12-15 | 2023-06-22 | ExxonMobil Technology and Engineering Company | Bulk cobalt-molybdenum catalyst compositions and synthesis methods |
US11746299B1 (en) | 2022-07-11 | 2023-09-05 | Saudi Arabian Oil Company | Methods and systems for upgrading mixed pyrolysis oil to light aromatics over mixed metal oxide catalysts |
CN115475644B (en) * | 2022-09-15 | 2023-09-19 | 青岛科技大学 | Method for preparing hydrogenated rosin by rosin hydrogenation and catalyst thereof |
Family Cites Families (54)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US480563A (en) * | 1892-08-09 | Sectional horseshoe | ||
NL78907C (en) * | 1951-08-31 | |||
US3520796A (en) * | 1968-08-21 | 1970-07-14 | Gulf Research Development Co | Making lubricating oils by hydrotreating and dewaxing |
US3678124A (en) * | 1968-10-24 | 1972-07-18 | Gennady Arkadievich Stepanov | Process for the production of mono- and diolefin hydrocarbons |
US3619414A (en) * | 1969-02-19 | 1971-11-09 | Sun Oil Co | Catalytic hydrofinishing of petroleum distillates in the lubricating oil boiling range |
US3861005A (en) * | 1969-05-28 | 1975-01-21 | Sun Oil Co Pennsylvania | Catalytic isomerization of lube streams and waxes |
US3901828A (en) * | 1971-11-08 | 1975-08-26 | Heraeus Gmbh W C | Oxidation catalyst for combustibles in gas mixtures |
GB1408759A (en) * | 1971-12-07 | 1975-10-01 | Shell Int Research | Catalytic hydrodesulphurisation process |
US3850746A (en) * | 1972-03-09 | 1974-11-26 | Exxon Research Engineering Co | Hydrodenitrogenation of hydrocarbon feedstocks with a catalyst composite of chrysotile and hydrogenation metal |
JPS5714333B2 (en) * | 1973-07-05 | 1982-03-24 | ||
IT1001977B (en) * | 1973-11-28 | 1976-04-30 | Sir Soc Italiana Resine Spa | PROCEDURE FOR THE PREPARATION OF METHYL ACRYLATE OR MIXTURES OF METHYL ACRYLATE AND ACRILIC ACID |
US4102822A (en) * | 1976-07-26 | 1978-07-25 | Chevron Research Company | Hydrocarbon hydroconversion catalyst and the method for its preparation |
US4388223A (en) * | 1981-04-06 | 1983-06-14 | Euteco Impianti S.P.A. | Catalyst for the conversion of unsaturated hydrocarbons into diolefins or unsaturated aldehydes and nitriles, and process for preparing the same |
US4395328A (en) * | 1981-06-17 | 1983-07-26 | Standard Oil Company (Indiana) | Catalyst and support, their methods of preparation, and processes employing same |
US4824821A (en) * | 1983-08-29 | 1989-04-25 | Chevron Research Company | Dispersed group VIB metal sulfide catalyst promoted with Group VIII metal |
US4857496A (en) * | 1983-08-29 | 1989-08-15 | Chevron Research Company | Heavy oil hydroprocessing with Group VI metal slurry catalyst |
FR2553680B1 (en) * | 1983-10-25 | 1987-09-18 | Inst Francais Du Petrole | CATALYSTS BASED ON GROUP VIII AND GROUP VIB METAL SULFIDES FOR HYDROPROCESSING REACTIONS OF SULFUR-CONTAINING HYDROCARBON CUTS |
EP0169054A3 (en) * | 1984-07-18 | 1987-12-16 | The University Of Newcastle Upon Tyne | Composite materials and products |
US4591429A (en) * | 1984-09-28 | 1986-05-27 | Exxon Research And Engineering Co. | Hydrotreating process employing catalysts comprising a supported mixture of a sulfide of a promoter metal, trivalent chromium and molybdenum or tungsten |
US4721558A (en) * | 1984-09-28 | 1988-01-26 | Exxon Research And Engineering Company | Hydrotreating catalysts comprising a mixture of a sulfide of a promoter metal amorphous sulfide of trivalent chromium and microcrystalline molybdenum or tungsten sulfide |
US4666878A (en) * | 1984-12-28 | 1987-05-19 | Exxon Research And Engineering Company | Amorphous, iron promoted Mo and W sulfide hydroprocessing catalysts and uses thereof |
GB8518940D0 (en) * | 1985-07-26 | 1985-09-04 | Shell Int Research | Manufacture of lubricating base oils |
EP0215989A1 (en) * | 1985-08-06 | 1987-04-01 | Exxon Research And Engineering Company | Amorphous, iron promoted mo and w sulfide hydroprocessing catalysts and uses thereof |
US4808563A (en) * | 1986-03-24 | 1989-02-28 | The Standard Oil Company | Molybdenum-tungsten-containing catalyst for methane conversion process |
JPS62199687A (en) * | 1986-04-28 | 1987-09-03 | ユニオン・オイル・コンパニ−・オブ・カリフオルニア | Hydrogenation using catalyst having large pores |
US4849093A (en) * | 1987-02-02 | 1989-07-18 | Union Oil Company Of California | Catalytic aromatic saturation of hydrocarbons |
US4875992A (en) * | 1987-12-18 | 1989-10-24 | Exxon Research And Engineering Company | Process for the production of high density jet fuel from fused multi-ring aromatics and hydroaromatics |
US4952306A (en) * | 1989-09-22 | 1990-08-28 | Exxon Research And Engineering Company | Slurry hydroprocessing process |
GB8925980D0 (en) * | 1989-11-16 | 1990-01-04 | Shell Int Research | Process for converting hydrocarbon oils |
US5122258A (en) * | 1991-05-16 | 1992-06-16 | Exxon Research And Engineering Company | Increasing VI of lube oil by hydrotreating using bulk Ni/Mn/Mo or Ni/Cr/Mo sulfide catalysts prepared from ligated metal complexes |
JPH04365526A (en) * | 1991-06-12 | 1992-12-17 | Kiwa Giken Kk | Grinding method and device thereof |
US5320741A (en) * | 1992-04-09 | 1994-06-14 | Stone & Webster Engineering Corporation | Combination process for the pretreatment and hydroconversion of heavy residual oils |
RU2030444C1 (en) * | 1992-07-20 | 1995-03-10 | Акционерное общество открытого типа "ЛУКойл-Пермнефтеоргсинтез" | Method of hydrotreatment of petroleum distillate fractions |
JP3057125B2 (en) * | 1992-10-02 | 2000-06-26 | 日石三菱株式会社 | Method for producing high viscosity index low viscosity lubricating base oil |
JP3065816B2 (en) * | 1992-10-02 | 2000-07-17 | 日石三菱株式会社 | Production method of high viscosity index low viscosity lubricating base oil |
US5306848A (en) * | 1992-10-16 | 1994-04-26 | Exxon Chemical Patents Inc. | Hydrogenation catalyst for oxo alcohol process |
DE4302991A1 (en) * | 1993-02-03 | 1994-08-04 | Basf Ag | Multimetal oxide materials |
JPH06262084A (en) * | 1993-03-12 | 1994-09-20 | Agency Of Ind Science & Technol | Hydrocracking catalyst of hydrocarbon oil |
JPH0782573A (en) * | 1993-07-23 | 1995-03-28 | Jgc Corp | Method and apparatus for treating petroleum |
US5399793A (en) * | 1993-11-29 | 1995-03-21 | Exxon Chemical Patents Inc. | Hydrogenation catalyst for oxo alcohol process |
US5382715A (en) * | 1993-11-29 | 1995-01-17 | Exxon Chemical Patents Inc. | Hydrogenation catalyst with low phosphorous content for oxo alcohol process |
US5510309A (en) * | 1994-05-02 | 1996-04-23 | Mobil Oil Corporation | Method for preparing a modified solid oxide |
KR100247525B1 (en) * | 1994-05-31 | 2000-03-15 | 겐지 아이다 | Catalyst for production of unsaturated aldehyde and unsaturated carboxylic acid and method for production of unsaturated aldehyde and unsaturated carboxylic acid by the use of the catalyst |
IT1275447B (en) * | 1995-05-26 | 1997-08-07 | Snam Progetti | PROCEDURE FOR THE CONVERSION OF HEAVY CRUDE AND DISTILLATION DISTILLATION RESIDUES |
JP3676849B2 (en) * | 1995-06-10 | 2005-07-27 | 財団法人石油産業活性化センター | Gas oil hydrodesulfurization catalyst |
US5911874A (en) * | 1996-06-28 | 1999-06-15 | Exxon Research And Engineering Co. | Raffinate hydroconversion process |
US5976353A (en) * | 1996-06-28 | 1999-11-02 | Exxon Research And Engineering Co | Raffinate hydroconversion process (JHT-9601) |
EP0912660A1 (en) * | 1996-07-15 | 1999-05-06 | Chevron U.S.A. Inc. | Layered catalyst system for lube oil hydroconversion |
EP0912659B1 (en) * | 1996-07-16 | 2003-09-10 | Chevron U.S.A. Inc. | Base stock lube oil manufacturing process |
US6096189A (en) * | 1996-12-17 | 2000-08-01 | Exxon Research And Engineering Co. | Hydroconversion process for making lubricating oil basestocks |
US6162350A (en) * | 1997-07-15 | 2000-12-19 | Exxon Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts (HEN-9901) |
US6156695A (en) * | 1997-07-15 | 2000-12-05 | Exxon Research And Engineering Company | Nickel molybdotungstate hydrotreating catalysts |
CN1055955C (en) * | 1997-11-24 | 2000-08-30 | 中国石油化工总公司 | Hydrogenation catalyst and preparation thereof |
US5968346A (en) * | 1998-09-16 | 1999-10-19 | Exxon Research And Engineering Co. | Two stage hydroprocessing with vapor-liquid interstage contacting for vapor heteroatom removal |
-
1999
- 1999-01-15 US US09/231,156 patent/US6162350A/en not_active Expired - Lifetime
-
2000
- 2000-01-14 CA CA2356920A patent/CA2356920C/en not_active Expired - Lifetime
- 2000-01-14 AU AU26137/00A patent/AU757716B2/en not_active Expired
- 2000-01-14 DE DE60040527T patent/DE60040527D1/en not_active Expired - Lifetime
- 2000-01-14 JP JP2000593687A patent/JP4766748B2/en not_active Expired - Lifetime
- 2000-01-14 DK DK00908284T patent/DK1169416T3/en active
- 2000-01-14 WO PCT/US2000/001008 patent/WO2000042121A1/en active IP Right Grant
- 2000-01-14 WO PCT/US2000/000992 patent/WO2000042129A1/en active IP Right Grant
- 2000-01-14 CN CNB008020418A patent/CN1136236C/en not_active Expired - Fee Related
- 2000-01-14 DK DK00908288.4T patent/DK1171547T3/en active
- 2000-01-14 AT AT00904366T patent/ATE388217T1/en not_active IP Right Cessation
- 2000-01-14 AU AU27276/00A patent/AU759434B2/en not_active Expired
- 2000-01-14 EP EP00906926A patent/EP1144351A1/en not_active Withdrawn
- 2000-01-14 DK DK00908286T patent/DK1169417T3/en active
- 2000-01-14 KR KR1020017008898A patent/KR20010101526A/en not_active Application Discontinuation
- 2000-01-14 WO PCT/US2000/000977 patent/WO2000041988A1/en not_active Application Discontinuation
- 2000-01-14 ES ES00908284T patent/ES2246828T3/en not_active Expired - Lifetime
- 2000-01-14 JP JP2000593686A patent/JP4524044B2/en not_active Expired - Lifetime
- 2000-01-14 AU AU29665/00A patent/AU763909B2/en not_active Ceased
- 2000-01-14 DE DE60014040T patent/DE60014040T2/en not_active Expired - Lifetime
- 2000-01-14 EP EP00904366A patent/EP1153106B1/en not_active Expired - Lifetime
- 2000-01-14 EP EP00905623A patent/EP1169414B1/en not_active Expired - Lifetime
- 2000-01-14 AT AT00909912T patent/ATE277149T1/en not_active IP Right Cessation
- 2000-01-14 CA CA2357022A patent/CA2357022C/en not_active Expired - Lifetime
- 2000-01-14 AU AU32095/00A patent/AU759972B2/en not_active Ceased
- 2000-01-14 BR BR0007821-2A patent/BR0007821A/en not_active IP Right Cessation
- 2000-01-14 AU AU26135/00A patent/AU757449B2/en not_active Expired
- 2000-01-14 JP JP2000593685A patent/JP2002534585A/en active Pending
- 2000-01-14 DK DK00905623T patent/DK1169414T3/en active
- 2000-01-14 WO PCT/US2000/001004 patent/WO2000042128A1/en active IP Right Grant
- 2000-01-14 CA CA002360035A patent/CA2360035A1/en not_active Abandoned
- 2000-01-14 JP JP2000593648A patent/JP2002534569A/en not_active Withdrawn
- 2000-01-14 DE DE60022176T patent/DE60022176T2/en not_active Expired - Lifetime
- 2000-01-14 AT AT00905623T patent/ATE411372T1/en not_active IP Right Cessation
- 2000-01-14 AU AU29663/00A patent/AU759864B2/en not_active Expired
- 2000-01-14 AT AT00908284T patent/ATE302831T1/en not_active IP Right Cessation
- 2000-01-14 WO PCT/US2000/000980 patent/WO2000042120A1/en active IP Right Grant
- 2000-01-14 AU AU29667/00A patent/AU762503B2/en not_active Ceased
- 2000-01-14 JP JP2000593558A patent/JP2002534264A/en not_active Withdrawn
- 2000-01-14 DE DE60026977T patent/DE60026977T2/en not_active Expired - Lifetime
- 2000-01-14 WO PCT/US2000/000981 patent/WO2000042125A1/en active IP Right Grant
- 2000-01-14 AU AU29662/00A patent/AU755642B2/en not_active Expired
- 2000-01-14 CA CA2359192A patent/CA2359192C/en not_active Expired - Lifetime
- 2000-01-14 CA CA2358695A patent/CA2358695C/en not_active Expired - Lifetime
- 2000-01-14 CA CA2358905A patent/CA2358905C/en not_active Expired - Lifetime
- 2000-01-14 CA CA2357024A patent/CA2357024C/en not_active Expired - Lifetime
- 2000-01-14 ES ES00908286T patent/ES2261183T3/en not_active Expired - Lifetime
- 2000-01-14 BR BR0007558-2A patent/BR0007558A/en not_active IP Right Cessation
- 2000-01-14 EP EP00905627A patent/EP1169415A4/en not_active Ceased
- 2000-01-14 EP EP00908284A patent/EP1169416B1/en not_active Expired - Lifetime
- 2000-01-14 DE DE60044244T patent/DE60044244D1/en not_active Expired - Lifetime
- 2000-01-14 AT AT00908288T patent/ATE465225T1/en not_active IP Right Cessation
- 2000-01-14 WO PCT/US2000/000898 patent/WO2000042082A1/en active IP Right Grant
- 2000-01-14 AU AU28506/00A patent/AU2850600A/en not_active Abandoned
- 2000-01-14 AT AT00908287T patent/ATE388216T1/en not_active IP Right Cessation
- 2000-01-14 WO PCT/US2000/000994 patent/WO2000042127A1/en active IP Right Grant
- 2000-01-14 AT AT00908286T patent/ATE321830T1/en not_active IP Right Cessation
- 2000-01-14 EP EP00904343A patent/EP1153046B1/en not_active Expired - Lifetime
- 2000-01-14 DK DK00909912T patent/DK1157083T3/en active
- 2000-01-14 WO PCT/US2000/001007 patent/WO2000042131A1/en active IP Right Grant
- 2000-01-14 AU AU29666/00A patent/AU763406B2/en not_active Ceased
- 2000-01-14 EP EP00908287A patent/EP1171549B1/en not_active Expired - Lifetime
- 2000-01-14 DE DE60038227T patent/DE60038227T2/en not_active Expired - Lifetime
- 2000-01-14 CA CA2356909A patent/CA2356909C/en not_active Expired - Lifetime
- 2000-01-14 WO PCT/US2000/000979 patent/WO2000042124A1/en active IP Right Grant
- 2000-01-14 JP JP2000593684A patent/JP4625582B2/en not_active Expired - Fee Related
- 2000-01-14 DE DE60019400T patent/DE60019400T2/en not_active Expired - Fee Related
- 2000-01-14 EP EP00904363A patent/EP1169413A4/en not_active Withdrawn
- 2000-01-14 CA CA2357528A patent/CA2357528C/en not_active Expired - Lifetime
- 2000-01-14 AU AU27280/00A patent/AU762701B2/en not_active Expired
- 2000-01-14 CA CA2358901A patent/CA2358901C/en not_active Expired - Lifetime
- 2000-01-14 JP JP2000593683A patent/JP4766747B2/en not_active Expired - Lifetime
- 2000-01-14 JP JP2000593679A patent/JP2002534580A/en active Pending
- 2000-01-14 JP JP2000593688A patent/JP5039256B2/en not_active Expired - Fee Related
- 2000-01-14 JP JP2000593678A patent/JP4681735B2/en not_active Expired - Lifetime
- 2000-01-14 WO PCT/US2000/001009 patent/WO2000042119A1/en active IP Right Grant
- 2000-01-14 EP EP00908283A patent/EP1169411A4/en active Pending
- 2000-01-14 JP JP2000593690A patent/JP4766749B2/en not_active Expired - Lifetime
- 2000-01-14 ES ES00905623T patent/ES2316351T3/en not_active Expired - Lifetime
- 2000-01-14 EP EP00908286A patent/EP1169417B1/en not_active Expired - Lifetime
- 2000-01-14 EP EP00908288A patent/EP1171547B1/en not_active Expired - Lifetime
- 2000-01-14 JP JP2000593680A patent/JP4766746B2/en not_active Expired - Lifetime
- 2000-01-14 EP EP00909912A patent/EP1157083B1/en not_active Expired - Lifetime
- 2000-01-14 CA CA2358910A patent/CA2358910C/en not_active Expired - Lifetime
- 2000-01-14 WO PCT/US2000/000993 patent/WO2000042126A1/en not_active Application Discontinuation
- 2000-01-14 MX MXPA01007139A patent/MXPA01007139A/en unknown
- 2000-01-14 DE DE60038223T patent/DE60038223D1/en not_active Expired - Lifetime
-
2001
- 2001-07-10 NO NO20013424A patent/NO20013424D0/en not_active Application Discontinuation
- 2001-07-10 NO NO20013425A patent/NO20013425L/en not_active Application Discontinuation
- 2001-07-10 NO NO20013417A patent/NO20013417L/en not_active Application Discontinuation
- 2001-07-13 NO NO20013491A patent/NO20013491L/en unknown
- 2001-07-13 NO NO20013488A patent/NO20013488L/en not_active Application Discontinuation
- 2001-07-13 NO NO20013490A patent/NO329317B1/en not_active IP Right Cessation
- 2001-07-13 NO NO20013485A patent/NO20013485L/en not_active Application Discontinuation
- 2001-07-13 NO NO20013489A patent/NO20013489L/en not_active Application Discontinuation
- 2001-07-13 NO NO20013486A patent/NO331510B1/en not_active IP Right Cessation
- 2001-07-13 NO NO20013487A patent/NO329318B1/en not_active IP Right Cessation
- 2001-07-13 NO NO20013492A patent/NO329323B1/en not_active IP Right Cessation
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2357528A1 (en) | Hydrotreating using bulk group viii/group vib catalysts | |
JP3387700B2 (en) | Desulfurization method of catalytic cracking gasoline | |
AU2003279190B2 (en) | Process for the production of high quality base oils | |
US3459656A (en) | Making a white oil by two stages of catalytic hydrogenation | |
CA3046985C (en) | Multistage resid hydrocracking | |
JP4785250B2 (en) | Production of low sulfur / low aromatic distillate | |
US5316658A (en) | Process for the production of low-sulfur diesel gas oil | |
US6531054B1 (en) | Process for effecting deep HDS of hydrocarbon feedstocks | |
CN103059938A (en) | Heavy hydrocarbon hydrotreating method | |
Absi-Halabi et al. | Performance comparison of alumina-supported Ni-Mo, Ni-W and Ni-Mo-W catalysis in hydrotreating vacuum residue | |
CA1334183C (en) | Process for hydrocracking of a hydrocarbon feedstock | |
CN109722292B (en) | Hydrocracking method for producing crude white oil | |
KR100808041B1 (en) | Process to prepare water-white lubricant base oil | |
CN101492614B (en) | Refining method for vaseline hydrogenation | |
US4769129A (en) | Method for hydroprocessing hydrocarbon-based charges | |
CN102443428B (en) | Heavy-hydrocarbon hydrogenation treatment method | |
KR950005958A (en) | Hydrogenation process of heavy oil | |
CN103131470B (en) | Fixed bed residue oil hydrotreating method | |
CA2402126C (en) | Production of low sulfur/low aromatics distillates | |
GB1191471A (en) | Integral Hydrocracking-Hydrotreating Process | |
GB1316080A (en) | Process for selectively hydrogenating petroleum cuts of the gasoline range in a plurality of steps | |
SEKI et al. | Deactivation of Hydrodesulfurization Catalysts in Two-stage Resid Desulfurization Process (Part 3) Influence of Asphaltene Content of Feedstock and Hydrodesulfurization Temperature at Second-stage | |
CN109722300B (en) | Hydrogenation method for producing crude white oil | |
EP0744452A2 (en) | Process for producing lubricating base oils | |
Fujikawa et al. | Cosmo high-activity hds catalyst: its development and performance properties |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKEX | Expiry |
Effective date: 20200114 |