RU2015117485A - Комплексная гидроочистка - Google Patents
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- 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
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- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
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- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
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- 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
- C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
- C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
- C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
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- 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
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- 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
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- 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
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- 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
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/12—Liquefied petroleum gas
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
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- C—CHEMISTRY; METALLURGY
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0244—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being an autothermal reforming step, e.g. secondary reforming processes
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- C—CHEMISTRY; METALLURGY
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/06—Integration with other chemical processes
- C01B2203/062—Hydrocarbon production, e.g. Fischer-Tropsch process
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/08—Methods of heating or cooling
- C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
- C01B2203/0833—Heating by indirect heat exchange with hot fluids, other than combustion gases, product gases or non-combustive exothermic reaction product gases
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1022—Fischer-Tropsch products
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
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- General Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1. Способ, включающий:фракционирование сырой нефти, конденсата или их смеси в установке фракционирования с получением фракционированного продукта, содержащего дизельное топливо, керосин или их смесь;использование синтез-газа в реакторе Фишера-Тропша с получением одного или нескольких продуктов процесса Фишера-Тропша; игидроочистку по меньшей мере части фракционированного продукта и по меньшей мере части продуктов процесса Фишера-Тропша в той же самой установке гидроочистки; где соотношение фракционированного продукта к продукту Фишера-Тропша составляет от примерно 0,5:1 до примерно 5:1 на основе массы, и где установка гидроочистки функционально соединена с установкой фракционирования и реактором Фишера-Тропша.2. Способ по п. 1, который дополнительно включает генерацию тепла в ходе осуществления реакции Фишера-Тропша и передачу по меньшей мере части упомянутого тепла к установке фракционирования.3. Способ по п. 1, который дополнительно включает конверсию природного газа в синтез-газ, где по меньшей мере часть упомянутого синтез-газа используется в ходе осуществления реакции Фишера-Тропша.4. Способ по п. 1, в котором упомянутая гидроочистка включает гидрирование, гидрокрекинг, гидроизомеризацию или гидрообработку.5. Способ по п. 1, в котором синтез-газ получают из установки для автотермического риформинга, установки для парового риформинга метана или установки для частичного окислительного риформинга.6. Способ по п. 1, в котором в ходе гидроочистки получают нафту, дизельное топливо, газойли, СНГ (сжиженный нефтяной газ), керосин, топливо для реактивных двигателей или их смесь.7. Комплексная система для конверсии газа в жидкости и
Claims (11)
1. Способ, включающий:
фракционирование сырой нефти, конденсата или их смеси в установке фракционирования с получением фракционированного продукта, содержащего дизельное топливо, керосин или их смесь;
использование синтез-газа в реакторе Фишера-Тропша с получением одного или нескольких продуктов процесса Фишера-Тропша; и
гидроочистку по меньшей мере части фракционированного продукта и по меньшей мере части продуктов процесса Фишера-Тропша в той же самой установке гидроочистки; где соотношение фракционированного продукта к продукту Фишера-Тропша составляет от примерно 0,5:1 до примерно 5:1 на основе массы, и где установка гидроочистки функционально соединена с установкой фракционирования и реактором Фишера-Тропша.
2. Способ по п. 1, который дополнительно включает генерацию тепла в ходе осуществления реакции Фишера-Тропша и передачу по меньшей мере части упомянутого тепла к установке фракционирования.
3. Способ по п. 1, который дополнительно включает конверсию природного газа в синтез-газ, где по меньшей мере часть упомянутого синтез-газа используется в ходе осуществления реакции Фишера-Тропша.
4. Способ по п. 1, в котором упомянутая гидроочистка включает гидрирование, гидрокрекинг, гидроизомеризацию или гидрообработку.
5. Способ по п. 1, в котором синтез-газ получают из установки для автотермического риформинга, установки для парового риформинга метана или установки для частичного окислительного риформинга.
6. Способ по п. 1, в котором в ходе гидроочистки получают нафту, дизельное топливо, газойли, СНГ (сжиженный нефтяной газ), керосин, топливо для реактивных двигателей или их смесь.
7. Комплексная система для конверсии газа в жидкости и фракционирования сырой нефти или конденсата, включающая:
установку фракционирования с получением фракционированного продукта, содержащего дизельное топливо, керосин или их смесь из сырой нефти, конденсата или их смеси;
реактор Фишера-Тропша для получения одного или нескольких продуктов процесса Фишера-Тропша из синтез-газа; и
установку гидроочистки, функционально соединенную с установкой фракционирования и реактором Фишера-Тропша таким образом, что установка гидроочистки способна осуществлять гидроочистку по меньшей мере части фракционированного продукта и по меньшей мере части продуктов процесса Фишера-Тропша.
8. Система по п. 7, которая дополнительно включает реактор Фишера-Тропша, функционально соединенный с установкой фракционирования таким образом, что по меньшей мере часть любого тепла, генерируемого в ходе осуществления реакции Фишера-Тропша, можно передать к установке фракционирования.
9. Система по п. 7, в которой на одной или нескольких установке фракционирования, реакторе Фишера-Тропша и установке гидроочистки применяют модульные технологии.
10. Система по п. 7, в которой на двух или нескольких установке фракционирования, реакторе Фишера-Тропша и установке гидроочистки применяют модульные технологии.
11. Система по п. 7, в которой на установке фракционирования, реакторе Фишера-Тропша и установке гидроочистки применяют модульные технологии.
Applications Claiming Priority (9)
Application Number | Priority Date | Filing Date | Title |
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US201261711714P | 2012-10-09 | 2012-10-09 | |
US201261711696P | 2012-10-09 | 2012-10-09 | |
US61/711,696 | 2012-10-09 | ||
US61/711,714 | 2012-10-09 | ||
US201361766924P | 2013-02-20 | 2013-02-20 | |
US61/766,924 | 2013-02-20 | ||
US13/838,266 US20140097123A1 (en) | 2012-10-09 | 2013-03-15 | Integrated hydroprocessing |
US13/838,266 | 2013-03-15 | ||
PCT/US2013/063923 WO2014058907A1 (en) | 2012-10-09 | 2013-10-08 | Integrated hydroprocessing |
Publications (1)
Publication Number | Publication Date |
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RU2015117485A true RU2015117485A (ru) | 2016-12-10 |
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RU2015117485A RU2015117485A (ru) | 2012-10-09 | 2013-10-08 | Комплексная гидроочистка |
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US (1) | US20140097123A1 (ru) |
CN (1) | CN104755597A (ru) |
AU (1) | AU2013329453A1 (ru) |
BR (1) | BR112015007845A2 (ru) |
CA (1) | CA2887688A1 (ru) |
MX (1) | MX2015004534A (ru) |
RU (1) | RU2015117485A (ru) |
WO (1) | WO2014058907A1 (ru) |
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US9815692B2 (en) * | 2014-07-28 | 2017-11-14 | Fluor Technologies Corporation | Configurations and method of integrating a gas to liquids (GTL) plant in a refinery |
WO2018206729A1 (en) * | 2017-05-11 | 2018-11-15 | Shell Internationale Research Maatschappij B.V. | Process for preparing an automotive gas oil fraction |
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US2134882A (en) * | 1935-07-26 | 1938-11-01 | Standard Oil Co | Fractionating apparatus and method of fractionation |
US3366460A (en) * | 1964-03-11 | 1968-01-30 | Chemical Construction Corp | Apparatus for exothermic catalytic reactions |
US5470457A (en) * | 1994-06-17 | 1995-11-28 | Phillips Petroleum Company | Stabilization of hydrocarbons by the addition of hydrazine |
EP1414931B1 (en) * | 2001-08-08 | 2011-12-14 | Shell Internationale Research Maatschappij B.V. | Process to prepare a hydrocarbon product having a sulphur content of below 0.05 wt % |
US7374657B2 (en) * | 2004-12-23 | 2008-05-20 | Chevron Usa Inc. | Production of low sulfur, moderately aromatic distillate fuels by hydrocracking of combined Fischer-Tropsch and petroleum streams |
FR2913024B1 (fr) * | 2007-02-27 | 2012-07-27 | Total France | Procede d'hydrotraitement d'une charge gazole, unite d'hydrotraitement pour la mise en oeuvre dudit procede, et unite d'hydroraffinage correspondante |
US7837857B2 (en) * | 2007-12-24 | 2010-11-23 | Uop Llc | Hydrocracking process for fabricating jet fuel from diesel fuel |
US8058492B2 (en) * | 2008-03-17 | 2011-11-15 | Uop Llc | Controlling production of transportation fuels from renewable feedstocks |
CN101928599B (zh) * | 2009-06-25 | 2015-04-29 | 中国石油化工股份有限公司 | 一种生产喷气燃料或喷气燃料调合组分的方法 |
US8932453B2 (en) * | 2010-07-23 | 2015-01-13 | Phillips 66 Company | Hydroprocessing process with improved catalyst activity |
US9169443B2 (en) * | 2011-04-20 | 2015-10-27 | Expander Energy Inc. | Process for heavy oil and bitumen upgrading |
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2013
- 2013-03-15 US US13/838,266 patent/US20140097123A1/en not_active Abandoned
- 2013-10-08 MX MX2015004534A patent/MX2015004534A/es unknown
- 2013-10-08 BR BR112015007845A patent/BR112015007845A2/pt not_active IP Right Cessation
- 2013-10-08 WO PCT/US2013/063923 patent/WO2014058907A1/en active Application Filing
- 2013-10-08 RU RU2015117485A patent/RU2015117485A/ru unknown
- 2013-10-08 CA CA2887688A patent/CA2887688A1/en not_active Abandoned
- 2013-10-08 AU AU2013329453A patent/AU2013329453A1/en not_active Abandoned
- 2013-10-08 CN CN201380056769.9A patent/CN104755597A/zh active Pending
Also Published As
Publication number | Publication date |
---|---|
BR112015007845A2 (pt) | 2017-07-04 |
CN104755597A (zh) | 2015-07-01 |
CA2887688A1 (en) | 2014-04-17 |
AU2013329453A1 (en) | 2015-04-30 |
MX2015004534A (es) | 2016-01-20 |
WO2014058907A1 (en) | 2014-04-17 |
US20140097123A1 (en) | 2014-04-10 |
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