RU2012156272A - Способ и устройство для получения углеводородов из сырья, содержащего талловое масло и терпеновые соединения - Google Patents
Способ и устройство для получения углеводородов из сырья, содержащего талловое масло и терпеновые соединения Download PDFInfo
- Publication number
- RU2012156272A RU2012156272A RU2012156272/04A RU2012156272A RU2012156272A RU 2012156272 A RU2012156272 A RU 2012156272A RU 2012156272/04 A RU2012156272/04 A RU 2012156272/04A RU 2012156272 A RU2012156272 A RU 2012156272A RU 2012156272 A RU2012156272 A RU 2012156272A
- Authority
- RU
- Russia
- Prior art keywords
- hydrotreating
- hydrocarbon components
- reactor
- isomerization
- tall oil
- Prior art date
Links
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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/42—Catalytic treatment
- C10G3/44—Catalytic treatment characterised by the catalyst used
- C10G3/45—Catalytic treatment characterised by the catalyst used containing iron group metals or compounds thereof
- C10G3/46—Catalytic treatment characterised by the catalyst used containing iron group metals or compounds thereof in combination with chromium, molybdenum, 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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/50—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids in the presence of hydrogen, hydrogen donors or hydrogen generating compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
-
- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/883—Molybdenum and nickel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/2206—Catalytic processes not covered by C07C5/23 - C07C5/31
- C07C5/226—Catalytic processes not covered by C07C5/23 - C07C5/31 with metals
-
- 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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/42—Catalytic treatment
- C10G3/44—Catalytic treatment characterised by the catalyst used
- C10G3/48—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support
-
- 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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/42—Catalytic treatment
- C10G3/44—Catalytic treatment characterised by the catalyst used
- C10G3/48—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support
- C10G3/49—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support containing crystalline aluminosilicates, 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
- C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
- C10G3/54—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids characterised by the catalytic bed
-
- 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
-
- 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
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
-
- 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
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
- C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
- C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins characterised by the catalyst used
- C10G45/64—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins 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
- 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
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
- C10G65/043—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 change in the structural skeleton
-
- 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
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
- C10G2300/1014—Biomass of vegetal origin
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
-
- 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
-
- 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
- C10G2300/70—Catalyst aspects
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
-
- 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
- C10G2400/04—Diesel 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
- C10G2400/06—Gasoil
-
- 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
- C10G2400/08—Jet fuel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Materials Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1. Способ получения углеводородных компонентов, включающий:предоставление сырья, содержащего талловое масло и терпеновые соединенияподвергание сырья и питающего газообразного водорода гидроочистке в присутствии NiO/МоОкатализатора на носителе AlOдля получения углеводородных компонентов, включающих н-парафины, иподвергание углеводородных компонентов, включающих н-парафины, изомеризации в присутствии NiW катализатора на носителе цеолит-AlOи в присутствии водорода для образования смеси углеводородных компонентов.2. Способ по п.1, где терпеновые соединения получают из растений, терпеновых масел, донного остатка перегонки терпенов и ароматизаторов и/или парфюмерной промышленности.3. Способ по п.2, где сырье содержит сырое талловое масло и сырой сульфатный скипидар, полученные при сульфатной варке древесины.4. Способ по п.3, где сырое талловое масло очищают перед подверганием гидроочистке.5. Способ по любому из предшествующих пп., где часть смеси углеводородных компонентов, полученных при изомеризации, направляют обратно на гидроочистку.6. Способ по п.1, где гидроочистку осуществляют при температуре от приблизительно 280°С до приблизительно 500°С, предпочтительно от приблизительно 330°С до приблизительно 430°С.7. Способ по п.1, где изомеризацию осуществляют при температуре от приблизительно 280°С до приблизительно 500°С, предпочтительно от приблизительно 330°С до приблизительно 430°С.8. Способ по п.1, где гидроочистку осуществляют под давлением от приблизительно 3 до приблизительно 20 МПа, предпочтительно от приблизительно 3 до приблизительно 10 МПа.9. Способ по п.1, где изомеризацию осуществляют под давлением от приблизительно 3 д
Claims (21)
1. Способ получения углеводородных компонентов, включающий:
предоставление сырья, содержащего талловое масло и терпеновые соединения
подвергание сырья и питающего газообразного водорода гидроочистке в присутствии NiO/МоО3 катализатора на носителе Al2O3 для получения углеводородных компонентов, включающих н-парафины, и
подвергание углеводородных компонентов, включающих н-парафины, изомеризации в присутствии NiW катализатора на носителе цеолит-Al2O3 и в присутствии водорода для образования смеси углеводородных компонентов.
2. Способ по п.1, где терпеновые соединения получают из растений, терпеновых масел, донного остатка перегонки терпенов и ароматизаторов и/или парфюмерной промышленности.
3. Способ по п.2, где сырье содержит сырое талловое масло и сырой сульфатный скипидар, полученные при сульфатной варке древесины.
4. Способ по п.3, где сырое талловое масло очищают перед подверганием гидроочистке.
5. Способ по любому из предшествующих пп., где часть смеси углеводородных компонентов, полученных при изомеризации, направляют обратно на гидроочистку.
6. Способ по п.1, где гидроочистку осуществляют при температуре от приблизительно 280°С до приблизительно 500°С, предпочтительно от приблизительно 330°С до приблизительно 430°С.
7. Способ по п.1, где изомеризацию осуществляют при температуре от приблизительно 280°С до приблизительно 500°С, предпочтительно от приблизительно 330°С до приблизительно 430°С.
8. Способ по п.1, где гидроочистку осуществляют под давлением от приблизительно 3 до приблизительно 20 МПа, предпочтительно от приблизительно 3 до приблизительно 10 МПа.
9. Способ по п.1, где изомеризацию осуществляют под давлением от приблизительно 3 до приблизительно 20 МПа, предпочтительно от приблизительно 3 до приблизительно 10 МПа.
10. Способ по п.1, где скорость подачи сырья WHSV составляет 0,6-1,2.
11. Способ по п.1, где смесь углеводородных компонентов подвергают сепарации для разделения углеводородных фракций бензинового, дизельного, реактивного и лигроинового диапазона.
12. Устройство для получения углеводородных компонентов из включающего талловое масло и терпеновые соединения сырья, включающее
- один или несколько реакторов гидроочистки (1, 1'),
- впускной канал сырья (4) для введения сырья в один или несколько реакторов гидроочистки,
- впускной канал водорода (6) для введения водорода в один или несколько реакторов гидроочистки,
- выпускной канал продукта (8) для отведения углеводородных компонентов из одного или нескольких реакторов гидроочистки, где по меньшей мере один из реакторов гидроочистки содержит каталитический слой (3) катализатора депарафинизации, которым является NiW на цеолит-Al2O3 носителе.
13. Устройство по п.12, где первый каталитический слой (3') NiO/МоО3 катализатора на Al2O3 носителе и второй каталитический слой (3) NiW катализатора на цеолит-Al2O3 носителе расположены в реакторе гидроочистки (1), первый каталитический слой (3') расположен выше по потоку от второго каталитического слоя (3).
14. Устройство по п.13, где устройство включает трубопровод рециркуляции продукта (80) для циркуляции потока продукта из смеси углеводородных компонентов, полученного из реактора (1), обратно в реактор (1).
15. Устройство по п.12, где первый каталитический слой (3') NiO/МоО3 катализатора на Al2O3 носителе расположен в первом реакторе гидроочистки (1'), и второй каталитический слой (3) NiW катализатора на цеолит-Al2O3 носителе расположен во втором реакторе гидроочистки (1), первый реактор (1') размещен выше по потоку от второго реактора (1).
16. Устройство по п.15, где устройство включает трубопровод рециркуляции продукта (80) для циркуляции потока продукта из смеси углеводородных компонентов, полученного из второго реактора (1), в первый реактор (1').
17. Устройство по любому из пп.12-16, где устройство содержит секцию очистки (13), которая расположена выше по потоку от по меньшей мере одного реактора гидроочистки (1, 1').
18. Устройство по п.12, где устройство включает сепаратор (2) для разделения углеводородных фракций бензинового, дизельного, реактивного и лигроинового диапазона.
19. Устройство по п.18, где тяжелую углеводородную фракцию удаляют из сепаратора и направляют по кругу в первый реактор через канал (11).
20. Применение углеводородных компонентов, полученных способом по любому из пп.1-11 в качестве топлива или в качестве присадки в топливные композиции.
21. Применение NiW катализатора на цеолит-Al2O3 носителе для изомеризации н-парафинов, полученных при гидроочистке сырья, содержащего талловое масло и терпеновые соединения.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20105583 | 2010-05-25 | ||
FI20105583A FI125632B (fi) | 2010-05-25 | 2010-05-25 | Menetelmä ja laite hiilivetyjen tuottamiseksi |
PCT/FI2011/050462 WO2011148046A1 (en) | 2010-05-25 | 2011-05-23 | Process and apparatus for producing hydrocarbons from feedstocks comprising tall oil and terpene-compounds |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2012156272A true RU2012156272A (ru) | 2014-06-27 |
RU2566763C2 RU2566763C2 (ru) | 2015-10-27 |
Family
ID=42234363
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2012156272/04A RU2566763C2 (ru) | 2010-05-25 | 2011-05-23 | Способ и устройство для получения углеводородов из сырья, содержащего талловое масло и терпеновые соединения |
Country Status (8)
Country | Link |
---|---|
US (1) | US9382483B2 (ru) |
EP (1) | EP2576732A1 (ru) |
CN (2) | CN103003392A (ru) |
BR (1) | BR112012029964B1 (ru) |
CA (1) | CA2800478C (ru) |
FI (1) | FI125632B (ru) |
RU (1) | RU2566763C2 (ru) |
WO (1) | WO2011148046A1 (ru) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103842478B (zh) | 2011-04-18 | 2015-12-23 | 芬欧汇川集团 | 用于由生物油生产烃类的催化方法和设备 |
FI126331B (en) | 2013-04-02 | 2016-10-14 | Upm Kymmene Corp | Renewable hydrocarbon composition |
FI126330B (en) | 2013-04-02 | 2016-10-14 | Upm Kymmene Corp | Renewable hydrocarbon composition |
FI126674B (en) * | 2013-07-12 | 2017-03-31 | Upm Kymmene Corp | Process for the preparation of hydrocarbons |
FI126812B (en) * | 2013-11-21 | 2017-05-31 | Upm Kymmene Corp | INTEGRATED PROCESS FOR THE PREPARATION OF HYDROCARBON |
US9682897B1 (en) * | 2015-04-30 | 2017-06-20 | The United States Of America As Represented By The Secretary Of The Navy | High density fuels from oxygenated terpenoids |
IT201700037970A1 (it) * | 2017-04-06 | 2018-10-06 | Eni Spa | Idrotrattamento di cariche da fonti rinnovabili con catalizzatori ad elevato contenuto di fase attiva |
CN108371932B (zh) * | 2017-12-29 | 2020-07-03 | 上海载正化工科技发展有限公司 | 一种制备小分子量聚苯醚的反应系统和方法 |
CA3011027C (en) | 2018-07-11 | 2022-08-09 | Suncor Energy Inc. | An integrated thermal system and process for heavy oil and gas to liquids conversion |
FI128115B2 (en) * | 2018-07-20 | 2024-08-20 | Neste Oyj | Cleaning of recycled and renewable organic material |
FI128069B2 (en) | 2018-07-20 | 2024-04-24 | Neste Oyj | Cleaning of recycled and renewable organic material |
FI128174B (en) | 2018-07-20 | 2019-11-29 | Neste Oyj | Purification of recycled and renewable organic material |
FI128911B (en) | 2018-07-20 | 2021-03-15 | Neste Oyj | Purification of recycled and renewable organic material |
FI128121B (en) | 2018-07-20 | 2019-10-15 | Neste Oyj | Production of hydrocarbons from recycled or renewable organic material |
FI20196039A1 (en) | 2019-11-29 | 2021-05-30 | Neste Oyj | Method of making a jet fuel component |
BR102019027610B1 (pt) | 2019-12-20 | 2022-03-08 | Petróleo Brasileiro S.A. – Petrobras | Processo seletivo para produção de combustíveis e destilados parafínicos de alto peso molecular renováveis e combustível |
FI129537B (en) | 2020-06-26 | 2022-04-14 | Upm Kymmene Corp | Multi-step procedure with hydrothermal liquefaction |
Family Cites Families (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3370099A (en) | 1962-12-12 | 1968-02-20 | Mobil Oil Corp | Isomerization process |
US3312750A (en) * | 1963-10-21 | 1967-04-04 | Berg Lloyd | Hydrodesulfurization of crude alpha-pinene |
CA2149685C (en) * | 1994-06-30 | 1999-09-14 | Jacques Monnier | Conversion of depitched tall oil to diesel fuel additive |
US6755963B2 (en) * | 1997-07-15 | 2004-06-29 | Exxonmobil Chemical Patents Inc. | Hydrogenation process for hydrocarbon resins |
US5959167A (en) | 1997-08-25 | 1999-09-28 | The University Of Utah Research Foundation | Process for conversion of lignin to reformulated hydrocarbon gasoline |
DE60312446T3 (de) * | 2002-09-06 | 2017-04-27 | Neste Oil Oyj | Vefahren zur Herstellung einer Kohlenwasserstoffkomponente biologischer Herkunft |
FI20021596A (fi) | 2002-09-06 | 2004-03-07 | Fortum Oyj | Dieselmoottorin polttoainekoostumus |
EA013998B1 (ru) | 2005-07-04 | 2010-08-30 | Несте Ойл Ойй | Способ производства углеводородов фракции дизельного топлива |
ES2550244T5 (es) | 2005-07-04 | 2023-06-08 | Neste Oyj | Proceso para la fabricación de hidrocarburos de la gama diésel |
WO2007064015A1 (ja) | 2005-11-30 | 2007-06-07 | Nippon Oil Corporation | 軽油組成物 |
US7578927B2 (en) | 2006-08-31 | 2009-08-25 | Uop Llc | Gasoline and diesel production from pyrolytic lignin produced from pyrolysis of cellulosic waste |
ITMI20062193A1 (it) | 2006-11-15 | 2008-05-16 | Eni Spa | Processo per produrre frazioni idrocarburiche da miscele di origine biologica |
MY146919A (en) | 2007-02-20 | 2012-10-15 | Shell Int Research | Process for producing paraffinic hydrocarbons |
FI121308B (fi) | 2007-06-11 | 2010-09-30 | Neste Oil Oyj | Prosessi haaroittuneiden hiilivetyjen valmistamiseksi |
US20080312480A1 (en) | 2007-06-15 | 2008-12-18 | E. I. Du Pont De Nemours And Company | Catalytic process for converting renewable resources into paraffins for use as diesel blending stocks |
US8742183B2 (en) | 2007-12-21 | 2014-06-03 | Uop Llc | Production of aviation fuel from biorenewable feedstocks |
US8894818B2 (en) | 2008-02-28 | 2014-11-25 | Chevron U.S.A. Inc. | Process for generating a hydrocarbon feedstock lignin |
US8193399B2 (en) * | 2008-03-17 | 2012-06-05 | Uop Llc | Production of diesel fuel and aviation fuel from renewable feedstocks |
US8735637B2 (en) * | 2008-04-21 | 2014-05-27 | Sunpine Ab | Conversion of crude tall oil to renewable feedstock for diesel range fuel compositions |
DK2141217T3 (en) * | 2008-07-01 | 2015-06-15 | Neste Oil Oyj | A process for producing jet fuel or blend stock for jet fuel of biological origin |
FI124508B (fi) | 2009-02-27 | 2014-09-30 | Upm Kymmene Oyj | Menetelmä ja laitteisto polttoainekomponenttien valmistamiseksi raakamäntyöljystä |
FI20095767A (fi) * | 2009-07-07 | 2011-01-08 | Upm Kymmene Corp | Menetelmä ja laite tärpätin konvertoimiseksi bensiinikomponenteiksi |
WO2011031630A2 (en) * | 2009-09-08 | 2011-03-17 | Exxonmobil Research And Engineering Company | Fuel production from feedstock containing lipidic material |
-
2010
- 2010-05-25 FI FI20105583A patent/FI125632B/fi active IP Right Grant
-
2011
- 2011-05-23 CN CN2011800306007A patent/CN103003392A/zh active Pending
- 2011-05-23 RU RU2012156272/04A patent/RU2566763C2/ru active
- 2011-05-23 CN CN201611221487.1A patent/CN106590722B/zh active Active
- 2011-05-23 CA CA2800478A patent/CA2800478C/en active Active
- 2011-05-23 BR BR112012029964-6A patent/BR112012029964B1/pt active IP Right Grant
- 2011-05-23 WO PCT/FI2011/050462 patent/WO2011148046A1/en active Application Filing
- 2011-05-23 US US13/699,542 patent/US9382483B2/en active Active
- 2011-05-23 EP EP11727716.0A patent/EP2576732A1/en active Pending
Also Published As
Publication number | Publication date |
---|---|
CA2800478A1 (en) | 2011-12-01 |
EP2576732A1 (en) | 2013-04-10 |
WO2011148046A1 (en) | 2011-12-01 |
US20130072730A1 (en) | 2013-03-21 |
FI20105583A (fi) | 2011-12-12 |
FI20105583L (fi) | 2011-12-12 |
CN106590722B (zh) | 2019-04-19 |
US9382483B2 (en) | 2016-07-05 |
CA2800478C (en) | 2018-01-02 |
BR112012029964A2 (pt) | 2016-09-20 |
RU2566763C2 (ru) | 2015-10-27 |
BR112012029964B1 (pt) | 2019-03-26 |
FI125632B (fi) | 2015-12-31 |
CN103003392A (zh) | 2013-03-27 |
CN106590722A (zh) | 2017-04-26 |
FI20105583A0 (fi) | 2010-05-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
RU2012156272A (ru) | Способ и устройство для получения углеводородов из сырья, содержащего талловое масло и терпеновые соединения | |
KR102613605B1 (ko) | 원유의 변환을 위한 시스템 및 공정 | |
CA2903354C (en) | Renewable hydrocarbon composition | |
RU2430957C2 (ru) | Способ и установка для конверсии тяжелых нефтяных фракций в кипящем слое интегрированным получением средних дистиллятов с очень низким содержанием серы | |
CA2915849C (en) | Process for producing hydrocarbons | |
FI126330B (en) | Renewable hydrocarbon composition | |
EP3071670B1 (en) | Integrated process for producing hydrocarbons | |
KR101973172B1 (ko) | 피셔-트롭슈 합성 오일을 이용한 디젤유 및 제트 연료 생산 시스템 및 방법 | |
CN102408295B (zh) | 甲醇制烯烃反应系统与烃类热解系统的整合 | |
FR2969642B1 (fr) | Production de carburants paraffiniques a partir de matieres renouvelables par un procede d'hydrotraitement en continu | |
JP2013515843A (ja) | 低純度の水素含有ストリームを用いたバイオ成分原材料の水素処理 | |
RU2015143892A (ru) | Гидрообработка продуктов термического крекинга | |
JP2022540531A (ja) | 合成ジェット燃料を製造する方法 | |
CA2767340A1 (en) | Process and apparatus for producing hydrocarbons | |
CN109988609B (zh) | 一种灵活页岩油加氢裂化工艺 | |
CN109988641B (zh) | 灵活页岩油加氢裂化工艺 | |
CN101724455B (zh) | 一种联合加氢方法 | |
CN105647580A (zh) | 费托合成全馏分油生产低凝中间馏分油系统及方法 | |
RU2009105660A (ru) | Способ десульфуризации углеводородов | |
CN109988635B (zh) | 一种加氢处理和加氢裂化组合工艺 | |
CN102863985A (zh) | 一种联合加氢方法 | |
RU2708252C1 (ru) | Способ и установка гидрирования парафинистой нефти | |
CN109988640B (zh) | 一种灵活加氢裂化工艺 | |
CN109777490B (zh) | 一种炼油厂气体加氢组合工艺 | |
CN109777517B (zh) | 一种炼油厂气体加氢组合方法 |