NO20091789L - Fremgangsmate for fremstilling av et raoljeprodukt - Google Patents
Fremgangsmate for fremstilling av et raoljeproduktInfo
- Publication number
- NO20091789L NO20091789L NO20091789A NO20091789A NO20091789L NO 20091789 L NO20091789 L NO 20091789L NO 20091789 A NO20091789 A NO 20091789A NO 20091789 A NO20091789 A NO 20091789A NO 20091789 L NO20091789 L NO 20091789L
- Authority
- NO
- Norway
- Prior art keywords
- crude oil
- oil product
- catalysts
- preparation
- residual content
- Prior art date
Links
- 239000010779 crude oil Substances 0.000 title abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 abstract 3
- 239000003054 catalyst Substances 0.000 abstract 3
- 229930195733 hydrocarbon Natural products 0.000 abstract 3
- 150000002430 hydrocarbons Chemical class 0.000 abstract 3
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000002184 metal Substances 0.000 abstract 1
- 239000011707 mineral Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 230000000737 periodic effect Effects 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
- C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
- C10G45/06—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
-
- 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
-
- 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
- B01J23/20—Vanadium, niobium or tantalum
- B01J23/22—Vanadium
-
- 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
- B01J23/70—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
- B01J23/882—Molybdenum and cobalt
-
- 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
- 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
- B01J35/34—Mechanical properties
- B01J35/37—Crush or impact strength
-
- 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
- B01J35/70—Catalysts, in general, characterised by their form or physical properties characterised by their crystalline properties, e.g. semi-crystalline
-
- 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
- C10G45/04—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
- C10G45/12—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 crystalline alumino-silicates, e.g. molecular sieves
-
- 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
-
- 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
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
-
- 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
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
- C10G49/04—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing nickel, cobalt, 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
- 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
-
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
-
- 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
- B01J2235/00—Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or 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
- B01J2235/00—Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties
- B01J2235/15—X-ray diffraction
-
- 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
- B01J2235/00—Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties
- B01J2235/30—Scanning electron microscopy; Transmission electron microscopy
-
- 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
- B01J35/61—Surface area
- B01J35/615—100-500 m2/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
- B01J35/63—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
- B01J35/66—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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
-
- 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
- B01J37/0201—Impregnation
- B01J37/0203—Impregnation the impregnation liquid containing organic compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/205—Metal content
- C10G2300/206—Asphaltenes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/208—Sediments, e.g. bottom sediment and water or BSW
-
- 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
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/308—Gravity, density, e.g. API
-
- 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
- C10G2300/4006—Temperature
-
- 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
- C10G2300/4012—Pressure
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Systemer, fremgangsmåter og katalysatorer for omdannelse av en hydrokarbontilførsel til et totalprodukt beskrives. Ved å bringe hydrokarbontilførselen i kontakt med en eller flere katalysatorer produseres totalproduktet. Dette innbefatter et råoljeprodukt som er en flytende blanding ved 25 °C og 0,101 MPa og som har et residuinnhold på høyst 90 % av residuinnholdet i hydrokarbontilførselen. Minst en av katalysatorene omfatter et metall fra kolonne 6 i det periodiske system, finoppdelt mineraloksid og en bærer.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US85010906P | 2006-10-06 | 2006-10-06 | |
PCT/US2007/080433 WO2008045757A2 (en) | 2006-10-06 | 2007-10-04 | Methods for producing a crude product |
Publications (1)
Publication Number | Publication Date |
---|---|
NO20091789L true NO20091789L (no) | 2009-07-03 |
Family
ID=38996723
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20091789A NO20091789L (no) | 2006-10-06 | 2009-05-05 | Fremgangsmate for fremstilling av et raoljeprodukt |
NO20091790A NO20091790L (no) | 2006-10-06 | 2009-05-05 | Fremgangsmate for fremstilling av et raoljeprodukt |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20091790A NO20091790L (no) | 2006-10-06 | 2009-05-05 | Fremgangsmate for fremstilling av et raoljeprodukt |
Country Status (10)
Country | Link |
---|---|
US (8) | US20080085225A1 (no) |
EP (8) | EP2073926A2 (no) |
JP (3) | JP2010506012A (no) |
KR (8) | KR20090085607A (no) |
CN (7) | CN101534939A (no) |
BR (8) | BRPI0717482A2 (no) |
CA (8) | CA2665631C (no) |
NO (2) | NO20091789L (no) |
RU (4) | RU2474607C2 (no) |
WO (8) | WO2008045760A1 (no) |
Families Citing this family (58)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100098602A1 (en) | 2003-12-19 | 2010-04-22 | Opinder Kishan Bhan | Systems, methods, and catalysts for producing a crude product |
US7745369B2 (en) | 2003-12-19 | 2010-06-29 | Shell Oil Company | Method and catalyst for producing a crude product with minimal hydrogen uptake |
US20050167327A1 (en) * | 2003-12-19 | 2005-08-04 | Bhan Opinder K. | Systems, methods, and catalysts for producing a crude product |
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 |
CN101166808B (zh) * | 2005-04-11 | 2013-03-27 | 国际壳牌研究有限公司 | 生产具有降低mcr含量的原油产品的方法和催化剂 |
US8435400B2 (en) * | 2005-12-16 | 2013-05-07 | Chevron U.S.A. | Systems and methods for producing a crude product |
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 |
US7931796B2 (en) | 2008-09-18 | 2011-04-26 | Chevron U.S.A. Inc. | 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 |
US8372266B2 (en) * | 2005-12-16 | 2013-02-12 | 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 |
US9512151B2 (en) | 2007-05-03 | 2016-12-06 | Auterra, Inc. | Product containing monomer and polymers of titanyls and methods for making same |
US9206359B2 (en) | 2008-03-26 | 2015-12-08 | Auterra, Inc. | Methods for upgrading of contaminated hydrocarbon streams |
US8298404B2 (en) | 2010-09-22 | 2012-10-30 | Auterra, Inc. | Reaction system and products therefrom |
US8894843B2 (en) | 2008-03-26 | 2014-11-25 | Auterra, Inc. | Methods for upgrading of contaminated hydrocarbon streams |
US9061273B2 (en) | 2008-03-26 | 2015-06-23 | Auterra, Inc. | Sulfoxidation catalysts and methods and systems of using same |
US8764973B2 (en) | 2008-03-26 | 2014-07-01 | Auterra, Inc. | Methods for upgrading of contaminated hydrocarbon streams |
KR20110018875A (ko) * | 2008-04-10 | 2011-02-24 | 셀 인터나쵸나아레 레사아치 마아츠샤피 비이부이 | 촉매 시스템 및 이 촉매 시스템으로 미정제 공급물을 변환시키는 방법 |
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 |
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 |
US8236169B2 (en) * | 2009-07-21 | 2012-08-07 | 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 |
US7897035B2 (en) | 2008-09-18 | 2011-03-01 | Chevron U.S.A. Inc. | Systems and methods for producing a crude product |
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 |
US8372268B2 (en) | 2009-03-24 | 2013-02-12 | Shell Oil Company | High surface area composition for use in the catalytic hydroconversion of a heavy hydrocarbon feedstock, a method making such composition and its use |
TWI511288B (zh) * | 2009-03-27 | 2015-12-01 | Semiconductor Energy Lab | 半導體裝置 |
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 |
US9523048B2 (en) | 2009-07-24 | 2016-12-20 | Lummus Technology Inc. | Pre-sulfiding and pre-conditioning of residuum hydroconversion catalysts for ebullated-bed hydroconversion processes |
US8840778B2 (en) * | 2010-03-29 | 2014-09-23 | Lyondell Chemical Technology, L.P. | Processing of acid containing hydrocarbons |
US9828557B2 (en) | 2010-09-22 | 2017-11-28 | Auterra, Inc. | Reaction system, methods and products therefrom |
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 |
HRP20240945T1 (hr) | 2010-12-30 | 2024-10-25 | Chevron U.S.A. Inc. | Katalizatori za hidropreradu i postupci njihove priprave |
KR101898289B1 (ko) * | 2011-01-10 | 2018-09-13 | 에스케이이노베이션 주식회사 | 탄화수소류 유분 내의 유기산을 저감하는 방법 |
US20130105357A1 (en) * | 2011-10-27 | 2013-05-02 | Shell Oil Company | Self-activating hydroprocessing catalyst and process for treating heavy hydrocarbon feedstocks |
EP2628780A1 (en) * | 2012-02-17 | 2013-08-21 | Reliance Industries Limited | A solvent extraction process for removal of naphthenic acids and calcium from low asphaltic crude oil |
US8999145B2 (en) | 2012-10-15 | 2015-04-07 | Uop Llc | Slurry hydrocracking process |
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 |
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 |
US9650312B2 (en) | 2013-03-14 | 2017-05-16 | Lummus Technology Inc. | Integration of residue hydrocracking and hydrotreating |
US10246647B2 (en) | 2015-03-26 | 2019-04-02 | Auterra, Inc. | Adsorbents and methods of use |
US10450516B2 (en) | 2016-03-08 | 2019-10-22 | Auterra, Inc. | Catalytic caustic desulfonylation |
TWI736610B (zh) * | 2016-04-25 | 2021-08-21 | 荷蘭商蜆殼國際研究所 | 用以降低沈降物產率之沸騰床工藝操作方法 |
TWI736611B (zh) * | 2016-04-25 | 2021-08-21 | 荷蘭商蜆殼國際研究所 | 用於在低沈降物量下高度轉化重烴之沸騰床方法 |
WO2017197346A1 (en) * | 2016-05-13 | 2017-11-16 | Gas Sensing Technology Corp. | Gross mineralogy and petrology using raman spectroscopy |
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 |
US20180230389A1 (en) | 2017-02-12 | 2018-08-16 | Magēmā Technology, LLC | Multi-Stage Process and Device for Reducing Environmental Contaminates in Heavy Marine Fuel Oil |
US12071592B2 (en) | 2017-02-12 | 2024-08-27 | Magēmā Technology LLC | Multi-stage process and device utilizing structured catalyst beds and reactive distillation for the production of a low sulfur heavy marine fuel oil |
US12025435B2 (en) | 2017-02-12 | 2024-07-02 | Magēmã Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil |
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 |
RU2636309C1 (ru) * | 2017-03-10 | 2017-11-22 | Федеральное государственное бюджетное учреждение науки Институт химии нефти Сибирского отделения Российской академии наук | Способ конверсии тяжелого нефтяного сырья |
CN108587675B (zh) * | 2018-03-29 | 2020-06-09 | 南京大学连云港高新技术研究院 | 一种重油减粘的方法 |
WO2021257538A1 (en) * | 2020-06-18 | 2021-12-23 | Chevron U.S.A. Inc. | Hydrocracking catalyst for heavy distillate |
US11975308B2 (en) * | 2020-06-19 | 2024-05-07 | Lg Chem, Ltd. | Dehydration catalyst, method for preparing the same, and method of preparing alkene using the same |
Family Cites Families (278)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1111580A (en) | 1914-02-09 | 1914-09-22 | Samuel M Herber | Oil distillation. |
GB496779A (en) | 1937-01-04 | 1938-12-06 | Bataafsche Petroleum | A process for removing naphthenic acids from mineral lubricating oils or lubricating oil fractions |
US2778777A (en) * | 1954-02-16 | 1957-01-22 | Texas Co | Removal of metal components from petroleum oils |
US2902429A (en) | 1955-06-17 | 1959-09-01 | California Research Corp | Demetallization of hydrocarbon fractions |
US2850435A (en) | 1956-02-06 | 1958-09-02 | Pure Oil Co | Method of removing high molecular weight naphthenic acids from hydrocarbon oils |
US2921023A (en) * | 1957-05-14 | 1960-01-12 | Pure Oil Co | Removal of naphthenic acids by hydrogenation with a molybdenum oxidesilica alumina catalyst |
NL267291A (no) * | 1959-05-14 | 1900-01-01 | ||
US3025231A (en) * | 1959-06-03 | 1962-03-13 | Texaco Inc | Catalytic hydrogenation of heavy oils such as shale oil |
NL264945A (no) | 1960-05-23 | |||
US3080435A (en) | 1960-07-18 | 1963-03-05 | Shell Oil Co | Dehydrogenation process |
NL121855C (no) * | 1960-08-29 | |||
NL275200A (no) | 1961-07-31 | |||
NL285285A (no) * | 1961-11-10 | |||
US3136715A (en) * | 1962-02-09 | 1964-06-09 | Jr Lloyd L Ames | Process of removing ruthenium from aqueous solutions |
GB1115122A (en) | 1965-08-23 | 1968-05-29 | Universal Oil Prod Co | Hydrotreatment of alkyl aromatic hydrocarbons |
US3488716A (en) | 1967-10-03 | 1970-01-06 | Exxon Research Engineering Co | Process for the removal of naphthenic acids from petroleum distillate fractions |
US3553279A (en) | 1968-03-29 | 1971-01-05 | Texas Instruments Inc | Method of producing ethylene |
US3617501A (en) | 1968-09-06 | 1971-11-02 | Exxon Research Engineering Co | Integrated process for refining whole crude oil |
US3558474A (en) * | 1968-09-30 | 1971-01-26 | Universal Oil Prod Co | Slurry process for hydrorefining petroleum crude oil |
US3547585A (en) | 1968-11-26 | 1970-12-15 | Universal Oil Prod Co | Combination of a hydrocarbon conversion process with a waste water treating process |
US3679577A (en) | 1968-11-29 | 1972-07-25 | Shell Oil Co | Molten salt hydrofining process |
US3576737A (en) | 1969-03-25 | 1971-04-27 | Chevron Res | Vanadium removal from hydrocarbons |
US3663431A (en) | 1969-10-15 | 1972-05-16 | Union Oil Co | Two-phase hydrocarbon conversion system |
GB1232173A (no) | 1969-11-18 | 1971-05-19 | ||
BE758565A (nl) * | 1969-11-18 | 1971-05-06 | Shell Int Research | Werkwijze voor het katalytisch hydrogenerend omzetten van een residualekoolwaterstofolie |
US3696027A (en) | 1970-01-12 | 1972-10-03 | Chevron Res | Multi-stage desulfurization |
US3622495A (en) | 1970-01-22 | 1971-11-23 | Universal Oil Prod Co | Multiple-stage slurry processing for black oil conversion |
US3716478A (en) * | 1970-02-10 | 1973-02-13 | Agency Ind Science Techn | Hydrogenation treatment of hydrocarbon oil |
GB1310283A (en) | 1970-06-12 | 1973-03-14 | Shell Int Research | Process for hydrogenative cracking of carbonaceous material |
GB1364238A (en) | 1970-08-04 | 1974-08-21 | Topsoe H F A | Process for the hydrodesulphurisation of heavy hydrocarbon oils |
US3745109A (en) | 1970-10-01 | 1973-07-10 | North American Rockwell | Hydrocarbon conversion process |
US3712861A (en) * | 1970-10-19 | 1973-01-23 | Mobil Oil Corp | Upgrading a hydrocarbon utilizing a catalyst of metal sulfides dispersed in alumina |
US3730876A (en) * | 1970-12-18 | 1973-05-01 | A Sequeira | Production of naphthenic oils |
US3766054A (en) | 1970-12-23 | 1973-10-16 | Mobil Oil Corp | Demetalation of hydrocarbon charge stocks |
US3716479A (en) * | 1970-12-23 | 1973-02-13 | Mobil Oil Corp | Demetalation of hydrocarbon charge stocks |
US3684688A (en) | 1971-01-21 | 1972-08-15 | Chevron Res | Heavy oil conversion |
US3677932A (en) | 1971-03-12 | 1972-07-18 | Shell Oil Co | Molten salt hydroconversion process |
US3812028A (en) * | 1971-05-18 | 1974-05-21 | Standard Oil Co | Hydrotreatment of fossil fuels |
US3786138A (en) * | 1971-08-16 | 1974-01-15 | Atlantic Richfield Co | Hydrogen generation |
US3847797A (en) | 1971-10-05 | 1974-11-12 | Exxon Research Engineering Co | Visbreaking a heavy hydrocarbon feedstock in a regenerable molten medium |
JPS5319071B2 (no) | 1971-10-18 | 1978-06-19 | ||
US3901792A (en) | 1972-05-22 | 1975-08-26 | Hydrocarbon Research Inc | Multi-zone method for demetallizing and desulfurizing crude oil or atmospheric residual oil |
US3876288A (en) * | 1972-09-08 | 1975-04-08 | West Electric Co | Light controlling device |
US3841981A (en) | 1972-12-29 | 1974-10-15 | Hydrocarbon Research Inc | Hydrogenation of tar sand bitumen |
JPS5139645B2 (no) * | 1972-12-30 | 1976-10-29 | ||
US3876532A (en) * | 1973-02-27 | 1975-04-08 | Gulf Research Development Co | Method for reducing the total acid number of a middle distillate oil |
US3948759A (en) * | 1973-03-28 | 1976-04-06 | Exxon Research And Engineering Company | Visbreaking a heavy hydrocarbon feedstock in a regenerable molten medium in the presence of hydrogen |
US3808122A (en) * | 1973-03-29 | 1974-04-30 | Chevron Res | Jet fuel by hydrocracking |
US3902991A (en) | 1973-04-27 | 1975-09-02 | Chevron Res | Hydrodesulfurization process for the production of low-sulfur hydrocarbon mixture |
US3960712A (en) | 1973-04-30 | 1976-06-01 | Universal Oil Products Company | Hydrodesulfurization of asphaltene-containing black oil with a gamma-alumina composite catalyst of specified particle density |
US3846288A (en) | 1973-07-05 | 1974-11-05 | Gulf Research Development Co | Acid number reduction of hydrocarbon fractions using a solid catalyst and methanol |
US3876523A (en) | 1973-08-29 | 1975-04-08 | Mobil Oil Corp | Catalyst for residua demetalation and desulfurization |
US3891541A (en) * | 1973-08-29 | 1975-06-24 | Mobil Oil Corp | Process for demetalizing and desulfurizing residual oil with hydrogen and alumina-supported catalyst |
US3931052A (en) | 1973-08-29 | 1976-01-06 | Mobil Oil Corporation | Alumina-supported catalyst for residua demetalation and desulfurization |
US3920538A (en) | 1973-11-30 | 1975-11-18 | Shell Oil Co | Demetallation with nickel-vanadium on silica in a hydrocarbon conversion process |
US3887455A (en) * | 1974-03-25 | 1975-06-03 | Exxon Research Engineering Co | Ebullating bed process for hydrotreatment of heavy crudes and residua |
US3928176A (en) | 1974-04-01 | 1975-12-23 | Exxon Research Engineering Co | Heavy crude conversion |
US3960706A (en) * | 1974-05-31 | 1976-06-01 | Standard Oil Company | Process for upgrading a hydrocarbon fraction |
SU1029830A3 (ru) * | 1974-05-31 | 1983-07-15 | Стандарт Ойл Компани (Фирма) | Способ получени углеводородных фракций из углеродсодержащего сырь |
US3960708A (en) * | 1974-05-31 | 1976-06-01 | Standard Oil Company | Process for upgrading a hydrocarbon fraction |
US3923635A (en) | 1974-06-17 | 1975-12-02 | Exxon Research Engineering Co | Catalytic upgrading of heavy hydrocarbons |
US4016067A (en) * | 1975-02-21 | 1977-04-05 | Mobil Oil Corporation | Process for demetalation and desulfurization of petroleum oils |
JPS51122105A (en) * | 1975-04-18 | 1976-10-26 | Toa Nenryo Kogyo Kk | Process for hydrofining of hydrocarbon oil |
US4062757A (en) | 1975-07-18 | 1977-12-13 | Gulf Research & Development Company | Residue thermal cracking process in a packed bed reactor |
US4196102A (en) * | 1975-12-09 | 1980-04-01 | Chiyoda Chemical Engineering & Construction Co., Ltd. | Catalysts for demetallization treatment of _hydrocarbons supported on sepiolite |
GB1561629A (en) * | 1975-12-10 | 1980-02-27 | Ici Ltd | Catalyst |
US4048060A (en) | 1975-12-29 | 1977-09-13 | Exxon Research And Engineering Company | Two-stage hydrodesulfurization of oil utilizing a narrow pore size distribution catalyst |
US4107087A (en) | 1976-03-31 | 1978-08-15 | Nalco Chemical Company | Use of citric acid to make catalyst from catalyst fines |
US4051015A (en) | 1976-06-11 | 1977-09-27 | Exxon Research & Engineering Co. | Hydroconversion of heavy hydrocarbons using copper chloride catalyst |
US4067799A (en) | 1976-07-02 | 1978-01-10 | Exxon Research And Engineering Company | Hydroconversion process |
JPS541306A (en) * | 1977-06-07 | 1979-01-08 | Chiyoda Chem Eng & Constr Co Ltd | Hydrogenation of heavy hydrocarbon oil |
US4115324A (en) | 1977-06-10 | 1978-09-19 | Nippon Mining Co., Ltd | Catalyst for treating heavy oils |
US4127470A (en) | 1977-08-01 | 1978-11-28 | Exxon Research & Engineering Company | Hydroconversion with group IA, IIA metal compounds |
US4119528A (en) | 1977-08-01 | 1978-10-10 | Exxon Research & Engineering Co. | Hydroconversion of residua with potassium sulfide |
US4271042A (en) | 1977-12-20 | 1981-06-02 | Mobil Oil Corporation | Process for demetalation and desulfurization of petroleum oils |
US4191635A (en) | 1977-12-21 | 1980-03-04 | Standard Oil Company (Indiana) | Process for the cracking of heavy hydrocarbon streams |
US4231858A (en) | 1978-06-15 | 1980-11-04 | Suntech, Inc. | Processing shale oil to jet fuel |
US4297242A (en) | 1978-07-26 | 1981-10-27 | Standard Oil Company (Indiana) | Process for demetallation and desulfurization of heavy hydrocarbons |
JPS5579043A (en) * | 1978-12-13 | 1980-06-14 | Chiyoda Chem Eng & Constr Co Ltd | Hydrogenation catalyst for heavy hydrocarbon oil |
JPS55102684A (en) | 1979-01-06 | 1980-08-06 | Mitsui Eng & Shipbuild Co Ltd | Thermal cracking of hydrocarbon and its device |
JPS55104920A (en) | 1979-01-30 | 1980-08-11 | Nippon Mining Co Ltd | Manufacture of lightened oil and hydrogen from heavy oil |
US4446244A (en) | 1979-09-26 | 1984-05-01 | Chevron Research Company | Hydrocarbons hydroprocessing with imogolite catalyst |
US4358361A (en) | 1979-10-09 | 1982-11-09 | Mobil Oil Corporation | Demetalation and desulfurization of oil |
US4357263A (en) | 1979-10-22 | 1982-11-02 | Mobil Oil Corporation | Catalyst for the upgrading of aromatic liquids |
CA1121293A (en) | 1979-11-26 | 1982-04-06 | Jaroslav F. Kriz | Catalytic hydrotreating or hydrocracking of hydrocarbon oils |
JPS595011B2 (ja) | 1979-11-27 | 1984-02-02 | 千代田化工建設株式会社 | 重質炭化水素油の水素化処理用触媒ならびにその製法 |
JPS601056B2 (ja) | 1980-02-19 | 1985-01-11 | 千代田化工建設株式会社 | アスファルテンを含む重質炭化水素油の水素化処理 |
US4324645A (en) | 1980-05-06 | 1982-04-13 | Mobil Oil Corporation | Upgrading residual oil |
US4306964A (en) | 1980-09-16 | 1981-12-22 | Mobil Oil Corporation | Multi-stage process for demetalation and desulfurization of petroleum oils |
FI803329L (fi) * | 1980-10-23 | 1982-04-24 | Farmos Oy | Vaextsubstratbaedd |
US4411824A (en) | 1981-05-12 | 1983-10-25 | Chevron Research Company | Method of making a catalyst suitable for hydrometalation of hydrocarbonaceous feedstocks |
US4549957A (en) | 1981-06-17 | 1985-10-29 | Amoco Corporation | Hydrotreating catalyst and process |
US4456699A (en) | 1981-06-17 | 1984-06-26 | Standard Oil Company (Indiana) | Catalyst and support, and their methods of preparation |
US4591426A (en) * | 1981-10-08 | 1986-05-27 | Intevep, S.A. | Process for hydroconversion and upgrading of heavy crudes of high metal and asphaltene content |
US4389301A (en) * | 1981-10-22 | 1983-06-21 | Chevron Research Company | Two-step hydroprocessing of heavy hydrocarbonaceous oils |
US4376037A (en) * | 1981-10-16 | 1983-03-08 | Chevron Research Company | Hydroprocessing of heavy hydrocarbonaceous oils |
US4427535A (en) | 1981-11-02 | 1984-01-24 | Hydrocarbon Research, Inc. | Selective operating conditions for high conversion of special petroleum feedstocks |
CA1209510A (en) | 1981-12-29 | 1986-08-12 | Chevron Research And Technology Company | Process for hydrodemetallation of hydrocarbon oils such as petroleum residua |
US4431525A (en) * | 1982-04-26 | 1984-02-14 | Standard Oil Company (Indiana) | Three-catalyst process for the hydrotreating of heavy hydrocarbon streams |
US4447314A (en) * | 1982-05-05 | 1984-05-08 | Mobil Oil Corporation | Demetalation, desulfurization, and decarbonization of petroleum oils by hydrotreatment in a dual bed system prior to cracking |
JPS58219293A (ja) | 1982-06-15 | 1983-12-20 | Chiyoda Chem Eng & Constr Co Ltd | 重質油の水素化分解方法 |
FR2528721B1 (fr) * | 1982-06-17 | 1986-02-28 | Pro Catalyse Ste Fse Prod Cata | Catalyseur supporte presentant une resistance accrue aux poisons et son utilisation en particulier pour l'hydrotraitement de fractions petrolieres contenant des metaux |
US4437980A (en) * | 1982-07-30 | 1984-03-20 | Rockwell International Corporation | Molten salt hydrotreatment process |
US4405441A (en) | 1982-09-30 | 1983-09-20 | Shell Oil Company | Process for the preparation of hydrocarbon oil distillates |
US4886594A (en) | 1982-12-06 | 1989-12-12 | Amoco Corporation | Hydrotreating catalyst and process |
US4450068A (en) * | 1982-12-20 | 1984-05-22 | Phillips Petroleum Company | Demetallization of hydrocarbon containing feed streams |
US4548710A (en) | 1982-12-28 | 1985-10-22 | Union Oil Company Of California | Hydrocarbon processing |
US4460707A (en) | 1982-12-28 | 1984-07-17 | Union Oil Company Of California | Hydroprocessing catalyst and method for preparing it |
FR2538813A1 (fr) * | 1982-12-31 | 1984-07-06 | Inst Francais Du Petrole | Procede d'hydrotraitement convertissant en au moins deux etapes une fraction lourde d'hydrocarbures contenant des impuretes soufrees et des impuretes metalliques |
JPS59132945A (ja) | 1983-01-21 | 1984-07-31 | Shokubai Kasei Kogyo Kk | 重質炭化水素油の水素化処理方法 |
US4592827A (en) * | 1983-01-28 | 1986-06-03 | Intevep, S.A. | Hydroconversion of heavy crudes with high metal and asphaltene content in the presence of soluble metallic compounds and water |
US4525472A (en) | 1983-02-23 | 1985-06-25 | Intevep, S.A. | Process for catalyst preparation for the hydrodemetallization of heavy crudes and residues |
US4473462A (en) | 1983-04-20 | 1984-09-25 | Chemroll Enterprises Inc | Treatment of petroleum and petroleum residues |
US4457836A (en) | 1983-05-13 | 1984-07-03 | Exxon Research And Engineering Company | Supported, non (metal-promoted) carbon-containing molybdenum sulfide catalysts for selective nitrogen removal |
FR2546175B1 (fr) | 1983-05-20 | 1989-12-22 | Intevep Sa | Procede de production d'un catalyseur d'hydrodemetallation de bruts lourds et de residus |
US4498979A (en) * | 1983-09-12 | 1985-02-12 | Exxon Research & Engineering Co. | Hydrodesulfurization process with conversion of heavy hydrocarbons utilizing a catalyst containing a group IIA metal component |
JPS6065093A (ja) * | 1983-09-21 | 1985-04-13 | Res Assoc Petroleum Alternat Dev<Rapad> | オイルサンド油および残渣油の処理方法 |
US4587012A (en) | 1983-10-31 | 1986-05-06 | Chevron Research Company | Process for upgrading hydrocarbonaceous feedstocks |
US4588709A (en) * | 1983-12-19 | 1986-05-13 | Intevep, S.A. | Catalyst for removing sulfur and metal contaminants from heavy crudes and residues |
US4520128A (en) * | 1983-12-19 | 1985-05-28 | Intevep, S.A. | Catalyst having high metal retention capacity and good stability for use in the demetallization of heavy crudes and method of preparation of same |
US4572778A (en) * | 1984-01-19 | 1986-02-25 | Union Oil Company Of California | Hydroprocessing with a large pore catalyst |
US4530757A (en) | 1984-03-29 | 1985-07-23 | Mobil Oil Corporation | Process for upgrading heavy crude oils |
US4560468A (en) | 1984-04-05 | 1985-12-24 | Phillips Petroleum Company | Hydrofining process for hydrocarbon containing feed streams |
CA1258439A (en) | 1984-04-16 | 1989-08-15 | Karl-Heinz W. Robschlager | Process for the catalytic conversion of heavy hydrocarbon oils |
JPS60227833A (ja) | 1984-04-27 | 1985-11-13 | Nippon Oil Co Ltd | 重質炭化水素油の水素化処理用触媒 |
JPS614533A (ja) * | 1984-06-15 | 1986-01-10 | Res Assoc Residual Oil Process<Rarop> | 水素化処理触媒およびこれを用いた重質鉱油の水素化脱硫分解方法 |
US4564439A (en) * | 1984-06-29 | 1986-01-14 | Chevron Research Company | Two-stage, close-coupled thermal catalytic hydroconversion process |
US4844792A (en) | 1984-08-07 | 1989-07-04 | Union Oil Company Of California | Hydroprocessing with a specific pore sized catalyst containing non-hydrolyzable halogen |
GB8425837D0 (en) * | 1984-10-12 | 1984-11-21 | Shell Int Research | Manufacture of lubricating base oils |
GB2167430B (en) | 1984-11-22 | 1988-11-30 | Intevep Sa | Process for hydroconversion and upgrading of heavy crudes of high metal and asphaltene content |
US4626412A (en) | 1984-12-14 | 1986-12-02 | Monsanto Company | Method and apparatus for carrying out catalyzed chemical reactions and for studying catalysts |
US5264183A (en) | 1984-12-14 | 1993-11-23 | Monsanto Company | Method and apparatus for carrying out catalyzed chemical reactions and for studying catalysis |
US4659454A (en) * | 1984-12-21 | 1987-04-21 | Mobil Oil Corporation | Hydrocracking of heavy feeds plus light fractions with dispersed dual function catalyst |
US4937222A (en) * | 1984-12-28 | 1990-06-26 | Mobil Oil Corporation | Catalyst capable of hydrotreating residual petroleum oil |
US4600503A (en) | 1984-12-28 | 1986-07-15 | Mobil Oil Corporation | Process for hydrotreating residual petroleum oil |
US4665261A (en) * | 1985-06-21 | 1987-05-12 | Atlantic Richfield Company | Hydrocarbon conversion process using a molten salt |
US5108581A (en) * | 1985-09-09 | 1992-04-28 | Exxon Research And Engineering Company | Hydroconversion of heavy feeds by use of both supported and unsupported catalysts |
US4661265A (en) | 1985-09-30 | 1987-04-28 | Amoco Corporation | Catalyst deoiling process |
US4746419A (en) * | 1985-12-20 | 1988-05-24 | Amoco Corporation | Process for the hydrodemetallation hydrodesulfuration and hydrocracking of a hydrocarbon feedstock |
US4729826A (en) | 1986-02-28 | 1988-03-08 | Union Oil Company Of California | Temperature controlled catalytic demetallization of hydrocarbons |
US4738884A (en) * | 1986-03-03 | 1988-04-19 | Owens-Corning Fiberglas Corporation | Asphalt adhesives superimposed on asphalt-based roofing sheet |
US4670134A (en) | 1986-05-02 | 1987-06-02 | Phillips Petroleum Company | Catalytic hydrofining of oil |
DE3623430A1 (de) * | 1986-07-11 | 1988-01-28 | Veba Oel Entwicklungs Gmbh | Verfahren zur hydrierenden behandlung von mit chlorbiphenylen u. dgl. kontaminierten mineraloelen |
US4830736A (en) * | 1986-07-28 | 1989-05-16 | Chevron Research Company | Graded catalyst system for removal of calcium and sodium from a hydrocarbon feedstock |
US5166118A (en) | 1986-10-08 | 1992-11-24 | Veba Oel Technologie Gmbh | Catalyst for the hydrogenation of hydrocarbon material |
DE3634275A1 (de) | 1986-10-08 | 1988-04-28 | Veba Oel Entwicklungs Gmbh | Verfahren zur hydrierenden konversion von schwer- und rueckstandsoelen |
US4917789A (en) * | 1987-02-03 | 1990-04-17 | Fina Technology, Inc. | Catalytic dewaxing process |
JPH0811184B2 (ja) | 1987-02-06 | 1996-02-07 | 日本石油株式会社 | 重質油の水素化処理触媒 |
DE3710021A1 (de) | 1987-03-30 | 1988-10-20 | Veba Oel Entwicklungs Gmbh | Verfahren zur hydrierenden konversion von schwer- und rueckstandsoelen |
DE3737370C1 (de) | 1987-11-04 | 1989-05-18 | Veba Oel Entwicklungs Gmbh | Verfahren zur hydrierenden Konversion von Schwer- und Rueckstandsoelen,Alt- und Abfalloelen in Mischung mit Klaerschlaemmen |
US5047142A (en) | 1988-05-13 | 1991-09-10 | Texaco Inc. | Catalyst composition and method for hydroprocessing petroleum feedstocks |
US4954473A (en) | 1988-07-18 | 1990-09-04 | Uop | Method of preparing a catalyst for the hydroconversion of asphaltene-containing hydrocarbonaceous charge stocks |
JP2631712B2 (ja) * | 1988-08-18 | 1997-07-16 | コスモ石油株式会社 | 重質炭化水素油の水素化処理触媒組成物ならびにそれを用いる水素化処理方法 |
US4992157A (en) | 1988-08-29 | 1991-02-12 | Uop | Process for improving the color and color stability of hydrocarbon fraction |
US4937218A (en) * | 1988-09-06 | 1990-06-26 | Intevep, S.A. | Catalytic system for the hydroconversion of heavy oils |
US5089463A (en) * | 1988-10-04 | 1992-02-18 | Chevron Research And Technology Company | Hydrodemetalation and hydrodesulfurization catalyst of specified macroporosity |
US4976848A (en) | 1988-10-04 | 1990-12-11 | Chevron Research Company | Hydrodemetalation and hydrodesulfurization using a catalyst of specified macroporosity |
DE68911856T2 (de) | 1988-10-19 | 1994-06-01 | Res Ass Petroleum Alternat Dev | Verfahren zur Hydrogenierung von Schwerölen. |
US4937221A (en) * | 1989-06-09 | 1990-06-26 | Institute Of Gas Technology | Mixed-solid solution tri-metallic oxide/sulfide catalyst and process for its preparation |
US5124024A (en) * | 1989-11-20 | 1992-06-23 | Nova Husky Research Corporation | Method for extending hydroconversion catalyst life |
US5124027A (en) | 1989-07-18 | 1992-06-23 | Amoco Corporation | Multi-stage process for deasphalting resid, removing catalyst fines from decanted oil and apparatus therefor |
US5916529A (en) | 1989-07-19 | 1999-06-29 | Chevron U.S.A. Inc | Multistage moving-bed hydroprocessing reactor with separate catalyst addition and withdrawal systems for each stage, and method for hydroprocessing a hydrocarbon feed stream |
US4992163A (en) * | 1989-12-13 | 1991-02-12 | Exxon Research And Engineering Company | Cat cracking feed preparation |
US4988434A (en) | 1989-12-13 | 1991-01-29 | Exxon Research And Engineering Company | Removal of metallic contaminants from a hydrocarbonaceous liquid |
US5024750A (en) | 1989-12-26 | 1991-06-18 | Phillips Petroleum Company | Process for converting heavy hydrocarbon oil |
US5164078A (en) | 1989-12-28 | 1992-11-17 | Chevron Research And Technology Company | Process for removal of calcium from a hydrocarbon feedstock |
US5216418A (en) * | 1990-03-13 | 1993-06-01 | Golden West Communications, Inc. | Emergency service rescue marker |
US5039489A (en) | 1990-04-17 | 1991-08-13 | Gleaves John T | Apparatus for catalyst analysis |
EP0460300A1 (en) * | 1990-06-20 | 1991-12-11 | Akzo Nobel N.V. | Process for the preparation of a presulphided catalyst; Process for the preparation of a sulphided catalyst, and use of said catalyst |
US5089453A (en) | 1990-06-25 | 1992-02-18 | Chevron Research And Technology Company | Hydroconversion catalyst and method for making the catalyst |
US5053117A (en) | 1990-07-25 | 1991-10-01 | Mobil Oil Corporation | Catalytic dewaxing |
US5851381A (en) | 1990-12-07 | 1998-12-22 | Idemitsu Kosan Co., Ltd. | Method of refining crude oil |
US5200060A (en) * | 1991-04-26 | 1993-04-06 | Amoco Corporation | Hydrotreating process using carbides and nitrides of group VIB metals |
US5358634A (en) | 1991-07-11 | 1994-10-25 | Mobil Oil Corporation | Process for treating heavy oil |
US5374350A (en) | 1991-07-11 | 1994-12-20 | Mobil Oil Corporation | Process for treating heavy oil |
US5215954A (en) | 1991-07-30 | 1993-06-01 | Cri International, Inc. | Method of presulfurizing a hydrotreating, hydrocracking or tail gas treating catalyst |
US5171727A (en) * | 1991-08-26 | 1992-12-15 | Uop | Method of preparing a catalyst for the hydroconversion of asphaltene-containing hydrocarbonaceous charge stocks |
US5474977A (en) | 1991-08-26 | 1995-12-12 | Uop | Catalyst for the hydroconversion of asphaltene-containing hydrocarbonaceous charge stocks |
US5210061A (en) | 1991-09-24 | 1993-05-11 | Union Oil Company Of California | Resid hydroprocessing catalyst |
US5215955A (en) * | 1991-10-02 | 1993-06-01 | Chevron Research And Technology Company | Resid catalyst with high metals capacity |
JP2966985B2 (ja) | 1991-10-09 | 1999-10-25 | 出光興産株式会社 | 重質炭化水素油の接触水素化処理方法 |
US5320741A (en) | 1992-04-09 | 1994-06-14 | Stone & Webster Engineering Corporation | Combination process for the pretreatment and hydroconversion of heavy residual oils |
US5223472A (en) * | 1992-04-14 | 1993-06-29 | Union Oil Company Of California | Demetallation catalyst |
US5399259A (en) | 1992-04-20 | 1995-03-21 | Texaco Inc. | Hydroconversion process employing catalyst with specified pore size distribution |
US5827421A (en) | 1992-04-20 | 1998-10-27 | Texaco Inc | Hydroconversion process employing catalyst with specified pore size distribution and no added silica |
EP0569092A1 (en) | 1992-05-05 | 1993-11-10 | Shell Internationale Researchmaatschappij B.V. | Hydrotreating process |
US5322617A (en) | 1992-08-07 | 1994-06-21 | Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Energy, Mines And Resources | Upgrading oil emulsions with carbon monoxide or synthesis gas |
US5300212A (en) * | 1992-10-22 | 1994-04-05 | Exxon Research & Engineering Co. | Hydroconversion process with slurry hydrotreating |
FR2701270B1 (fr) | 1993-02-08 | 1995-04-14 | Inst Francais Du Petrole | Procédé d'élimination du mercure dans les hydrocarbures par passage sur un catalyseur présulfuré. |
US5397456A (en) * | 1993-02-19 | 1995-03-14 | Texaco Inc. | Hydroconversion process employing catalyst with specified pore size distribution |
US5395536A (en) * | 1993-05-07 | 1995-03-07 | Baker Hughes, Inc. | Wastewater organic acid removal process |
US5462651A (en) | 1994-08-09 | 1995-10-31 | Texaco Inc. | Hydrodearomatization of hydrocarbon oils using novel "phosphorus treated carbon" supported metal sulfide catalysts |
US5514273A (en) * | 1993-10-01 | 1996-05-07 | Texaco Inc. | Hydroconversion process employing catalyst with specified pore size distribution |
US5928499A (en) | 1993-10-01 | 1999-07-27 | Texaco Inc | Hydroconversion process employing catalyst with specified pore size distribution, median pore diameter by surface area, and pore mode by volume |
US5468371A (en) | 1994-04-11 | 1995-11-21 | Texaco Inc. | Catalyst for residual conversion demonstrating reduced toluene insolubles |
US5620592A (en) * | 1994-07-29 | 1997-04-15 | Chevron U.S.A. Inc. | Low macropore resid conversion catalyst |
NO303837B1 (no) * | 1994-08-29 | 1998-09-07 | Norske Stats Oljeselskap | FremgangsmÕte for Õ fjerne hovedsakelig naftensyrer fra en hydrokarbonolje |
JP3504984B2 (ja) | 1994-09-19 | 2004-03-08 | 日本ケッチェン株式会社 | 重質炭化水素油の水素化脱硫脱金属触媒 |
DE19600684A1 (de) * | 1995-02-17 | 1996-08-22 | Linde Ag | Verfahren zum Spalten von Kohlenwasserstoffen und Vorrichtung |
US5885441A (en) * | 1997-04-11 | 1999-03-23 | Intevep, S.A. | Steam conversion process and catalyst |
US5635056A (en) | 1995-05-02 | 1997-06-03 | Exxon Research And Engineering Company | Continuous in-situ process for upgrading heavy oil using aqueous base |
US5961815A (en) | 1995-08-28 | 1999-10-05 | Catalytic Distillation Technologies | Hydroconversion process |
US5807469A (en) * | 1995-09-27 | 1998-09-15 | Intel Corporation | Flexible continuous cathode contact circuit for electrolytic plating of C4, tab microbumps, and ultra large scale interconnects |
US5817229A (en) | 1995-11-06 | 1998-10-06 | Texaco Inc | Catalytic hydrocarbon upgrading process requiring no external hydrogen supply |
AU1959997A (en) | 1996-02-14 | 1997-09-02 | Texaco Development Corporation | Low pressure process for the hydroconversion of heavy hydrocarbo ns |
US6210564B1 (en) * | 1996-06-04 | 2001-04-03 | Exxon Research And Engineering Company | Process for desulfurization of petroleum feeds utilizing sodium metal |
US5856609A (en) * | 1996-09-12 | 1999-01-05 | Phillips Petroleum Company | Aromatic hydrodealkylation process with sulfur oxide containing catalyst |
FR2753982B1 (fr) * | 1996-10-02 | 1999-05-28 | Inst Francais Du Petrole | Procede catalytique en plusieurs etapes de conversion d'une fraction lourde d'hydrocarbures |
DE69711348T2 (de) * | 1996-12-17 | 2002-10-24 | Inst Francais Du Petrol | Bor und Silicium enthaltender Katalysator und Anwendung dieses in der Hydrobehandlung von Kohlenwasserstoffeinsätzen |
US6086749A (en) | 1996-12-23 | 2000-07-11 | Chevron U.S.A. Inc. | Catalyst and method for hydroprocessing a hydrocarbon feed stream in a reactor containing two or more catalysts |
FR2758278B1 (fr) | 1997-01-15 | 1999-02-19 | Inst Francais Du Petrole | Catalyseur comprenant un sulfure mixte et utilisation en hydroraffinage et hydroconversion d'hydrocarbures |
US5744025A (en) * | 1997-02-28 | 1998-04-28 | Shell Oil Company | Process for hydrotreating metal-contaminated hydrocarbonaceous feedstock |
FR2764213B1 (fr) * | 1997-06-10 | 1999-07-16 | Inst Francais Du Petrole | Catalyseur d'hydrotraitement de charges hydrocarbonees dans un reacteur a lit fixe |
US6620313B1 (en) | 1997-07-15 | 2003-09-16 | Exxonmobil Research And Engineering Company | Hydroconversion process using bulk group VIII/Group VIB catalysts |
US6162350A (en) | 1997-07-15 | 2000-12-19 | Exxon Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts (HEN-9901) |
US6582590B1 (en) | 1997-07-15 | 2003-06-24 | Exxonmobil Research And Engineering Company | Multistage hydroprocessing using bulk multimetallic catalyst |
US6755963B2 (en) | 1997-07-15 | 2004-06-29 | Exxonmobil Chemical Patents Inc. | Hydrogenation process for hydrocarbon resins |
US6635599B1 (en) | 1997-07-15 | 2003-10-21 | Exxonmobil Research & Engineering Company | Mixed metal catalyst, its preparation by co-precipitation, and its use |
US5847249A (en) | 1997-07-28 | 1998-12-08 | Catalytic Distillation Technologies | Apparatus and process for catalytic distillations |
US5910242A (en) | 1997-08-29 | 1999-06-08 | Exxon Research And Engineering Company | Process for reduction of total acid number in crude oil |
US5928502A (en) | 1997-08-29 | 1999-07-27 | Exxon Research And Engineering Co. | Process for reducing total acid number of crude oil |
US5871636A (en) * | 1997-08-29 | 1999-02-16 | Exxon Research And Engineering Company | Catalytic reduction of acidity of crude oils in the absence of hydrogen |
US5897769A (en) | 1997-08-29 | 1999-04-27 | Exxon Research And Engineering Co. | Process for selectively removing lower molecular weight naphthenic acids from acidic crudes |
US5914030A (en) * | 1997-08-29 | 1999-06-22 | Exxon Research And Engineering. Co. | Process for reducing total acid number of crude oil |
ZA989153B (en) | 1997-10-15 | 1999-05-10 | Equistar Chem Lp | Method of producing olefins and feedstocks for use in olefin production from petroleum residua which have low pentane insolubles and high hydrogen content |
US5942101A (en) | 1997-12-09 | 1999-08-24 | Exxon Research And Engineering Co. | Method for decreasing the conradson carbon number of petroleum streams |
US5928501A (en) * | 1998-02-03 | 1999-07-27 | Texaco Inc. | Process for upgrading a hydrocarbon oil |
US6248230B1 (en) * | 1998-06-25 | 2001-06-19 | Sk Corporation | Method for manufacturing cleaner fuels |
US6096192A (en) | 1998-07-14 | 2000-08-01 | Exxon Research And Engineering Co. | Producing pipelinable bitumen |
FR2787041B1 (fr) | 1998-12-10 | 2001-01-19 | Inst Francais Du Petrole | Catalyseur d'hydrotraitement de charges hydrocarbonees dans un reacteur a lit fixe |
FR2787040B1 (fr) | 1998-12-10 | 2001-01-19 | Inst Francais Du Petrole | Hydrotraitement de charges hydrocarbonees dans un reacteur en lit bouillonnant |
US6534437B2 (en) | 1999-01-15 | 2003-03-18 | Akzo Nobel N.V. | Process for preparing a mixed metal catalyst composition |
JP4303820B2 (ja) | 1999-01-26 | 2009-07-29 | 日本ケッチェン株式会社 | 水素化処理用触媒並びに水素化処理方法 |
US7056422B2 (en) | 1999-01-27 | 2006-06-06 | Sector Capital Corporation | Batch thermolytic distillation of carbonaceous material |
US6218333B1 (en) | 1999-02-15 | 2001-04-17 | Shell Oil Company | Preparation of a hydrotreating catalyst |
US6554994B1 (en) * | 1999-04-13 | 2003-04-29 | Chevron U.S.A. Inc. | Upflow reactor system with layered catalyst bed for hydrotreating heavy feedstocks |
FR2792851B1 (fr) | 1999-04-29 | 2002-04-05 | Inst Francais Du Petrole | Catalyseur a base de metal noble faiblement disperse et son utilisation pour la conversion de charges hydrocarbonees |
GB9912842D0 (en) | 1999-06-02 | 1999-08-04 | Bp Exploration Operating | Process for reducing the acidity of oil |
AU2001229692A1 (en) | 2000-01-24 | 2001-07-31 | Arthur D. Little, Inc. | Apparatus and methods for conversion of hydrocarbon feed streams into liquid products |
US6509291B2 (en) * | 2000-04-11 | 2003-01-21 | Akzo Nobel N.V. | Process for sulfiding a catalyst containing an S-containing additive |
US6524469B1 (en) * | 2000-05-16 | 2003-02-25 | Trans Ionics Corporation | Heavy oil upgrading process |
RU2186090C2 (ru) | 2000-05-18 | 2002-07-27 | Королева Наталья Владиславовна | Способ получения жидких нефтепродуктов гидрогенизацией и деметаллизацией тяжелого нефтяного сырья |
WO2001094009A1 (fr) | 2000-06-08 | 2001-12-13 | Japan Energy Corporation | Procede de preparation d'un catalyseur utilise dans le raffinage par hydrogenation et procede de recuperation de metal |
JP2003171671A (ja) * | 2000-06-08 | 2003-06-20 | Japan Energy Corp | 重質油の水素化精製方法 |
US6203313B1 (en) * | 2000-06-09 | 2001-03-20 | Rebbecca L. Holmes | Candle having reconfigurable shape |
US6454932B1 (en) | 2000-08-15 | 2002-09-24 | Abb Lummus Global Inc. | Multiple stage ebullating bed hydrocracking with interstage stripping and separating |
US20020056664A1 (en) | 2000-09-07 | 2002-05-16 | Julie Chabot | Extension of catalyst cycle length in residuum desulfurization processes |
US6457994B1 (en) * | 2000-10-12 | 2002-10-01 | 3Com Corporation | Media connector that allows electrical communication to be established with a media plug |
US6547957B1 (en) * | 2000-10-17 | 2003-04-15 | Texaco, Inc. | Process for upgrading a hydrocarbon oil |
JP4260477B2 (ja) | 2000-10-24 | 2009-04-30 | 日揮株式会社 | 精製油およびその製造方法 |
JP2002129171A (ja) | 2000-10-27 | 2002-05-09 | Ngk Insulators Ltd | 重質油の分解方法 |
US20020112987A1 (en) | 2000-12-15 | 2002-08-22 | Zhiguo Hou | Slurry hydroprocessing for heavy oil upgrading using supported slurry catalysts |
RU2282784C2 (ru) * | 2001-04-20 | 2006-08-27 | Эксонмобил Апстрим Рисерч Компани | Способ и устройство для обогащения тяжелой нефти |
US20030042174A1 (en) * | 2001-06-18 | 2003-03-06 | Petronetiics Llc. | Method to treat emulsified hydrocarbon mixtures |
US6841062B2 (en) * | 2001-06-28 | 2005-01-11 | Chevron U.S.A. Inc. | Crude oil desulfurization |
CN1151235C (zh) | 2001-07-02 | 2004-05-26 | 中国石油化工股份有限公司 | 一种重烃类原料加氢处理方法及其反应器 |
WO2003025098A2 (en) | 2001-09-17 | 2003-03-27 | Southwest Research Institute | Pretreatment processes for heavy oil and carbonaceous materials |
US20030070808A1 (en) * | 2001-10-15 | 2003-04-17 | Conoco Inc. | Use of syngas for the upgrading of heavy crude at the wellhead |
US6759364B2 (en) | 2001-12-17 | 2004-07-06 | Shell Oil Company | Arsenic removal catalyst and method for making same |
US20030149317A1 (en) | 2002-02-04 | 2003-08-07 | Rendina David Deck | Hydrogenation catalysts and methods |
US7338795B2 (en) | 2002-03-11 | 2008-03-04 | Intevep, S.A. | Biodesulfurization of hydrocarbons |
US6808919B2 (en) | 2002-03-11 | 2004-10-26 | Intevep, S.A. | Biodesulfurization of hydrocarbons |
GB0209222D0 (en) | 2002-04-23 | 2002-06-05 | Bp Oil Int | Purification process |
JP2006512430A (ja) | 2002-12-06 | 2006-04-13 | アルベマーレ ネザーランズ ビー.ブイ. | 触媒の混合物を使用する炭化水素の水素化処理 |
NL1027771C2 (nl) * | 2003-12-19 | 2006-07-13 | Shell Int Research | Systemen, methoden en katalysatoren voor het produceren van een ruwe-oliehoudend product. |
US7763160B2 (en) * | 2003-12-19 | 2010-07-27 | Shell Oil Company | Systems and methods of producing a crude product |
US20070000810A1 (en) * | 2003-12-19 | 2007-01-04 | Bhan Opinder K | Method for producing a crude product with reduced tan |
US20070000808A1 (en) * | 2003-12-19 | 2007-01-04 | Bhan Opinder K | Method and catalyst for producing a crude product having selected properties |
US7745369B2 (en) * | 2003-12-19 | 2010-06-29 | Shell Oil Company | Method and catalyst for producing a crude product with minimal hydrogen uptake |
US20050167327A1 (en) | 2003-12-19 | 2005-08-04 | Bhan Opinder K. | Systems, methods, and catalysts for producing a crude product |
FR2866897B1 (fr) | 2004-03-01 | 2007-08-31 | Inst Francais Du Petrole | Utilisation de gaz pour le preraffinage de petrole conventionnel et optionnellement sequestration de co2 |
US20060060510A1 (en) * | 2004-09-17 | 2006-03-23 | Bhan Opinder K | High activity hydrodesulfurization catalyst, a method of making a high activity hydrodesulfurization catalyst, and a process for manufacturing an ultra-low sulfur distillate product |
TWI415930B (zh) | 2005-04-06 | 2013-11-21 | Shell Int Research | 減少液態含烴原料總酸值(tan)的方法 |
CN101166808B (zh) | 2005-04-11 | 2013-03-27 | 国际壳牌研究有限公司 | 生产具有降低mcr含量的原油产品的方法和催化剂 |
BRPI0609411A2 (pt) | 2005-04-11 | 2011-10-11 | Shell Int Research | método para produzir um produto bruto |
WO2006110595A1 (en) | 2005-04-11 | 2006-10-19 | Shell Internationale Research Maatschappij B.V. | Method and catalyst for producing a crude product having a reduced nitrogen content |
EP1874896A1 (en) | 2005-04-11 | 2008-01-09 | Shell International Research Maatschappij B.V. | Method and catalyst for producing a crude product having a reduced nitroge content |
JP2008535999A (ja) | 2005-04-11 | 2008-09-04 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | 原油生成物を製造するためのシステム、方法及び触媒 |
-
2007
- 2007-10-03 US US11/866,923 patent/US20080085225A1/en not_active Abandoned
- 2007-10-03 US US11/866,926 patent/US20080083655A1/en not_active Abandoned
- 2007-10-03 US US11/866,909 patent/US20080087578A1/en not_active Abandoned
- 2007-10-03 US US11/866,921 patent/US20090188836A1/en not_active Abandoned
- 2007-10-03 US US11/866,922 patent/US7749374B2/en not_active Expired - Fee Related
- 2007-10-03 US US11/866,929 patent/US20080083650A1/en not_active Abandoned
- 2007-10-03 US US11/866,916 patent/US20080087575A1/en not_active Abandoned
- 2007-10-03 US US11/866,932 patent/US20080135449A1/en not_active Abandoned
- 2007-10-04 CA CA2665631A patent/CA2665631C/en not_active Expired - Fee Related
- 2007-10-04 KR KR1020097009157A patent/KR20090085607A/ko not_active Application Discontinuation
- 2007-10-04 WO PCT/US2007/080440 patent/WO2008045760A1/en active Application Filing
- 2007-10-04 BR BRPI0717482-9A2A patent/BRPI0717482A2/pt not_active IP Right Cessation
- 2007-10-04 RU RU2009116445/04A patent/RU2474607C2/ru not_active IP Right Cessation
- 2007-10-04 JP JP2009531605A patent/JP2010506012A/ja not_active Withdrawn
- 2007-10-04 KR KR1020097009160A patent/KR20090102737A/ko not_active Application Discontinuation
- 2007-10-04 CN CNA200780042701XA patent/CN101534939A/zh active Pending
- 2007-10-04 CN CNA2007800427946A patent/CN101535448A/zh active Pending
- 2007-10-04 EP EP07853768A patent/EP2073926A2/en not_active Withdrawn
- 2007-10-04 KR KR1020097009162A patent/KR20090091698A/ko not_active Application Discontinuation
- 2007-10-04 BR BRPI0717480-2A2A patent/BRPI0717480A2/pt not_active IP Right Cessation
- 2007-10-04 CA CA2665545A patent/CA2665545C/en not_active Expired - Fee Related
- 2007-10-04 CA CA002665373A patent/CA2665373A1/en not_active Abandoned
- 2007-10-04 KR KR1020097009155A patent/KR20090085606A/ko not_active Application Discontinuation
- 2007-10-04 WO PCT/US2007/080413 patent/WO2008045750A2/en active Application Filing
- 2007-10-04 BR BRPI0717781-0A patent/BRPI0717781A2/pt not_active Application Discontinuation
- 2007-10-04 EP EP07853764A patent/EP2073925A2/en not_active Withdrawn
- 2007-10-04 CN CNA2007800429138A patent/CN101541421A/zh active Pending
- 2007-10-04 WO PCT/US2007/080429 patent/WO2008045755A1/en active Application Filing
- 2007-10-04 CN CNA2007800427274A patent/CN101583422A/zh active Pending
- 2007-10-04 BR BRPI0717478-0A2A patent/BRPI0717478A2/pt not_active Application Discontinuation
- 2007-10-04 WO PCT/US2007/080422 patent/WO2008045753A2/en active Application Filing
- 2007-10-04 EP EP07868368A patent/EP2074198A2/en not_active Withdrawn
- 2007-10-04 EP EP07853763A patent/EP2073924A2/en not_active Withdrawn
- 2007-10-04 KR KR1020097009159A patent/KR20090091697A/ko not_active Application Discontinuation
- 2007-10-04 RU RU2009117176/04A patent/RU2009117176A/ru not_active Application Discontinuation
- 2007-10-04 RU RU2009117172/04A patent/RU2448152C2/ru not_active IP Right Cessation
- 2007-10-04 EP EP07843832A patent/EP2073923A1/en not_active Withdrawn
- 2007-10-04 BR BRPI0717467-5A patent/BRPI0717467B1/pt not_active IP Right Cessation
- 2007-10-04 KR KR1020097009156A patent/KR20090102735A/ko not_active Application Discontinuation
- 2007-10-04 WO PCT/US2007/080410 patent/WO2008045749A2/en active Application Filing
- 2007-10-04 JP JP2009531604A patent/JP5735212B2/ja not_active Expired - Fee Related
- 2007-10-04 WO PCT/US2007/080407 patent/WO2008060779A2/en active Application Filing
- 2007-10-04 KR KR1020097009158A patent/KR20090102736A/ko not_active Application Discontinuation
- 2007-10-04 CN CN2007800427452A patent/CN101541420B/zh not_active Expired - Fee Related
- 2007-10-04 BR BRPI0717298-2A2A patent/BRPI0717298A2/pt not_active IP Right Cessation
- 2007-10-04 EP EP07853775A patent/EP2074197A2/en not_active Withdrawn
- 2007-10-04 BR BRPI0717479-9A2A patent/BRPI0717479A2/pt not_active IP Right Cessation
- 2007-10-04 CA CA002665479A patent/CA2665479A1/en not_active Abandoned
- 2007-10-04 CA CA002665548A patent/CA2665548A1/en not_active Abandoned
- 2007-10-04 CN CNA2007800428826A patent/CN101535449A/zh active Pending
- 2007-10-04 CA CA002665499A patent/CA2665499A1/en not_active Abandoned
- 2007-10-04 WO PCT/US2007/080435 patent/WO2008045758A1/en active Application Filing
- 2007-10-04 RU RU2009117168/04A patent/RU2009117168A/ru not_active Application Discontinuation
- 2007-10-04 WO PCT/US2007/080433 patent/WO2008045757A2/en active Application Filing
- 2007-10-04 EP EP07843827A patent/EP2073922A1/en not_active Withdrawn
- 2007-10-04 CA CA002665560A patent/CA2665560A1/en not_active Abandoned
- 2007-10-04 BR BRPI0717780-1A2A patent/BRPI0717780A2/pt not_active IP Right Cessation
- 2007-10-04 CA CA002665550A patent/CA2665550A1/en not_active Abandoned
- 2007-10-04 CN CN2007800429091A patent/CN101534940B/zh not_active Expired - Fee Related
- 2007-10-04 EP EP07853771A patent/EP2073927A1/en not_active Withdrawn
- 2007-10-04 KR KR1020097009161A patent/KR101547526B1/ko not_active IP Right Cessation
-
2009
- 2009-05-05 NO NO20091789A patent/NO20091789L/no not_active Application Discontinuation
- 2009-05-05 NO NO20091790A patent/NO20091790L/no not_active Application Discontinuation
-
2013
- 2013-08-12 JP JP2013167323A patent/JP2014012845A/ja active Pending
Also Published As
Similar Documents
Publication | Publication Date | Title |
---|---|---|
NO20091789L (no) | Fremgangsmate for fremstilling av et raoljeprodukt | |
NO20075767L (no) | Fremgangsmate og katalysator for fremstilling av et raoljeprodukt med et redusert nitrogeninnhold | |
NO20075770L (no) | Fremgangsmate og katalysator for fremstilling av et raoljeprodukt med et redusert innhold av MCR | |
WO2006110659A3 (en) | Systems, methods, and catalysts for producing a crude product | |
MX2020007371A (es) | Procedimiento de enriquecimiento de petroleo renovable que contiene oxigeno. | |
MX2019000422A (es) | Proceso para producir petroleo renovable que contiene oxigeno, bajo en azufre. | |
MX2009004139A (es) | Produccion de olefinas que utiliza la materia prima entera del petroleo crudo/condensado con produccion mejorada de destilado. | |
WO2009004181A3 (fr) | Production de charges de vapocraquage a haut rendement en ethylene, propylene et polymeres resultants par hydrotraitement d'huile vegetales | |
MY156207A (en) | Process for the conversion of ethane to aromatic hydrocarbons | |
WO2012005784A8 (en) | Solvent-enhanced biomass liquefaction | |
WO2009126974A3 (en) | Method for preparing a diluted hydrocarbon composition, and diluted hydrocarbon compositions | |
UA96572C2 (ru) | Способ, аппарат и установка для переработки органического материала в углеводородное топливо | |
GB2488678A (en) | A process for making products with low hydrogen halide | |
UA98537C2 (ru) | Процесс производства ароматических углеводородов | |
TW200728446A (en) | Olefin production utilizing whole crude oil feedstock | |
WO2011117705A3 (en) | Process for the conversion of lignin to liquid hydrocarbons | |
GB2460968A (en) | Method and system for recovering aromatics from a naphtha feedstock | |
RU2007141711A (ru) | Способ получения полупродукта с пониженным содержанием азота и катализатора для его осуществления | |
BR112018005995A2 (pt) | conversão de biomassa em metano | |
EP3201296B1 (en) | Process for producing aromatics from wide-boiling temperature hydrocarbon feedstocks | |
AR070235A1 (es) | Proceso para hidrodesulfurizar gasolina de fcc resultando en un producto con bajo contenido de mercaptanos | |
WO2011090610A3 (en) | Process for removing metals from crude oil | |
SG138599A1 (en) | System, methods, and catalysts for producing a crude product | |
WO2009065878A3 (en) | Method for the start-up of a catalytic process | |
BRPI0605675A (pt) | processo para conversão de etanol e hidrocarbonetos em uma unidade de craqueamento catalìtico fluido |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FC2A | Withdrawal, rejection or dismissal of laid open patent application |