RU2016136357A - Переработка остатка вакуумной дистилляции нефти и вакуумного газойля в системах реакторов с кипящим слоем - Google Patents
Переработка остатка вакуумной дистилляции нефти и вакуумного газойля в системах реакторов с кипящим слоем Download PDFInfo
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- RU2016136357A RU2016136357A RU2016136357A RU2016136357A RU2016136357A RU 2016136357 A RU2016136357 A RU 2016136357A RU 2016136357 A RU2016136357 A RU 2016136357A RU 2016136357 A RU2016136357 A RU 2016136357A RU 2016136357 A RU2016136357 A RU 2016136357A
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- Prior art keywords
- fluidized bed
- effluent
- oil
- hydrocarbon
- produce
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- 238000007670 refining Methods 0.000 title 1
- 238000005292 vacuum distillation Methods 0.000 title 1
- 150000002430 hydrocarbons Chemical group 0.000 claims 26
- 238000004517 catalytic hydrocracking Methods 0.000 claims 20
- 238000000034 method Methods 0.000 claims 19
- 229930195733 hydrocarbon Natural products 0.000 claims 18
- 239000004215 Carbon black (E152) Substances 0.000 claims 17
- 239000003921 oil Substances 0.000 claims 14
- 239000003054 catalyst Substances 0.000 claims 13
- 229910021536 Zeolite Inorganic materials 0.000 claims 12
- 239000010457 zeolite Substances 0.000 claims 12
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims 11
- 238000006243 chemical reaction Methods 0.000 claims 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 8
- 239000007789 gas Substances 0.000 claims 8
- 239000001257 hydrogen Substances 0.000 claims 8
- 229910052739 hydrogen Inorganic materials 0.000 claims 8
- 239000000047 product Substances 0.000 claims 8
- 239000007788 liquid Substances 0.000 claims 6
- 239000000463 material Substances 0.000 claims 6
- 239000010426 asphalt Substances 0.000 claims 5
- 238000005194 fractionation Methods 0.000 claims 5
- 229910052751 metal Inorganic materials 0.000 claims 5
- 239000002184 metal Substances 0.000 claims 5
- 238000009835 boiling Methods 0.000 claims 4
- 239000010779 crude oil Substances 0.000 claims 3
- 238000004821 distillation Methods 0.000 claims 3
- 239000012263 liquid product Substances 0.000 claims 3
- 239000002028 Biomass Substances 0.000 claims 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims 2
- 238000010521 absorption reaction Methods 0.000 claims 2
- 230000003197 catalytic effect Effects 0.000 claims 2
- -1 kerogen Substances 0.000 claims 2
- 239000010687 lubricating oil Substances 0.000 claims 2
- 239000000203 mixture Substances 0.000 claims 2
- 239000002808 molecular sieve Substances 0.000 claims 2
- 239000010815 organic waste Substances 0.000 claims 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims 2
- 239000003079 shale oil Substances 0.000 claims 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims 2
- 239000003784 tall oil Substances 0.000 claims 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims 1
- 238000005299 abrasion Methods 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 150000001720 carbohydrates Chemical class 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 239000003245 coal Substances 0.000 claims 1
- 229910017052 cobalt Inorganic materials 0.000 claims 1
- 239000010941 cobalt Substances 0.000 claims 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims 1
- 238000004939 coking Methods 0.000 claims 1
- 229910052675 erionite Inorganic materials 0.000 claims 1
- 239000012013 faujasite Substances 0.000 claims 1
- 238000005243 fluidization Methods 0.000 claims 1
- 239000000295 fuel oil Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 150000002739 metals Chemical class 0.000 claims 1
- 229910052750 molybdenum Inorganic materials 0.000 claims 1
- 239000011733 molybdenum Substances 0.000 claims 1
- 229910052680 mordenite Inorganic materials 0.000 claims 1
- 229910052759 nickel Inorganic materials 0.000 claims 1
- 229910000510 noble metal Inorganic materials 0.000 claims 1
- 239000010742 number 1 fuel oil Substances 0.000 claims 1
- 229910052763 palladium Inorganic materials 0.000 claims 1
- 229910052697 platinum Inorganic materials 0.000 claims 1
- 239000002994 raw material Substances 0.000 claims 1
- 239000011269 tar Substances 0.000 claims 1
- 239000011275 tar sand Substances 0.000 claims 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims 1
- 229910052721 tungsten Inorganic materials 0.000 claims 1
- 239000010937 tungsten Substances 0.000 claims 1
Classifications
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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
- 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
- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
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- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
- B01J8/222—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid in the presence of a rotating device only
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
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- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
- B01J8/224—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
- B01J8/226—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement internally, i.e. the particles rotate within the vessel
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- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
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- 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
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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
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- C10G47/14—Inorganic carriers the catalyst containing platinum group metals or compounds thereof
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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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- C10G47/16—Crystalline alumino-silicate carriers
- C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or compounds thereof
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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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- C10G47/24—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions with moving solid particles
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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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- 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
- C10G49/10—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 with moving solid particles
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- 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
- C10G49/10—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 with moving solid particles
- C10G49/16—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 with moving solid particles according to the "fluidised-bed" technique
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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
- 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
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- 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
- C10G65/10—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
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- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/06—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including a sorption process as the refining step in the absence of hydrogen
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- C10G2300/1003—Waste materials
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1074—Vacuum distillates
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- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1077—Vacuum residues
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Claims (43)
1. Способ повышения качества углеводородных остатков и тяжелого дистиллятного сырья, включающий:
введение в контакт углеводородных остатков и водорода с металлосодержащим катализатором гидропереработки на нецеолитной основе в первой системе реакторов гидропереработки в кипящем слое для получения первого выходящего потока;
фракционирование первого выходящего потока из первого реактора гидропереработки в кипящем слое для получения жидкого продукта и парового продукта;
введение в контакт парового продукта и тяжелого дистиллятного сырья с цеолитным селективным катализатором гидрокрекинга во второй системе реакторов гидрокрекинга в кипящем слое для получения второго выходящего потока;
выведение второго выходящего потока из второй системы реакторов гидрокрекинга в кипящем слое; и
фракционирование второго выходящего потока из второй системы реакторов гидрокрекинга в кипящем слое для получения одной или нескольких углеводородных фракций.
2. Способ по п.1, дополнительно включающий нагревание углеводородных остатков и водорода перед контактом с катализатором.
3. Способ по п.1, в котором в углеводородные остатки выбирают из одного или нескольких материалов, таких как сырая нефть, сланцевая нефть, битум из битуминозных песков, полученная из битумного угля нефть, талловое масло, смазочный мазут, органические отходы, полученные из биомассы жидкости или любая тяжелая фракция нефтяного остатка.
4. Способ по п.1, в котором тяжелое дистиллятное сырье выбирает из одного или нескольких материалов, таких как атмосферный газойль, легкий вакуумный газойль, тяжелый вакуумный газойль, тяжелый газойль коксования, рецикловый газойль каталитического крекинга в псевдоожиженном слое (FCC) и деасфальтированное масло, производимое из источников нефти, битума, керогена, биомассы или органических отходов.
5. Способ по п.4, в котором тяжелое дистиллятное сырье представляет собой прямогонный вакуумный газойль, получаемый как верхняя фракция сырой нефти, из которой получают углеводородные остатки.
6. Способ по п.1, в котором остаточная углеводородная фракция включает, по меньшей мере, один материал, такой как остатки дистилляции нефти при атмосферном давлении или в вакууме, деасфальтированные масла, пек из деасфальтизатора, подвергнутые гидрокрекингу нижние фракции работающей при атмосферном давлении или в вакууме колонны, подвергнутый каталитическому крекингу в псевдоожиженном слое (FCC) мазут, полученный из сланцевой нефти остаток, полученная из битумного угля нефть, сырая нефть биологического происхождения, битум из битуминозных песков, талловое масло, смазочный мазут.
7. Способ по п.1, в котором введение в контакт в первой системе реакторов гидропереработки в кипящем слое включает работу первой системы реакторов гидропереработки в кипящем слое в жестких условиях для достижения степени превращения углеводородов, составляющей, по меньшей мере, приблизительно 50 мас.% и степени деметаллизации, составляющей, по меньшей мере, 50%, причем степень превращения определяется как процентное уменьшение массы материалов, у которых температура кипения превышает 480°C по стандарту ASTM для дистилляции смесей тяжелых углеводородов.
8. Способ по п.1, в котором введение в контакт во второй системе реакторов гидрокрекинга в кипящем слое включает работу реакторов в жестких условиях для достижения степени превращения углеводородов, составляющей, по меньшей мере, приблизительно 60 мас.%, причем степень превращения определяется по образованию материалов, у которых температура кипения составляет менее чем приблизительно 370°C согласно стандарту ASTM D1160 для дистилляции смесей тяжелых углеводородов.
9. Способ по п.1, в котором цеолитный селективный катализатор гидропереработки включает, по меньшей мере, один материал, такой как H Y-цеолит, H ZSM-5, морденит, эрионит или сверхустойчивый фожазит, USY-цеолит, бета-цеолит, ZSM-11, ZSM-22, ZSM-23, ZSM-35, ZSM-48, ZSM-57, ZSM-34, молекулярное сито REY или молекулярное сито REHY.
10. Способ по п.9, в котором цеолитный селективный катализатор гидрокрекинга дополнительно включает один или несколько металлов, таких как кобальт, молибден, вольфрам, никель, платина или палладий.
11. Способ по п.1, в котором фракционирование первого выходящего потока из первой системы реакторов гидропереработки в кипящем слое для получения жидкого продукта и парового продукта дополнительно включает: введение в контакт парового продукта с углеводородным потоком для образования второго парового продукта и второго жидкого продукта и введение второго парового продукта в качестве парового продукта во вторую систему реакторов гидрокрекинга в кипящем слое.
12. Способ по п.11, в котором углеводородный поток представляет собой углеводородный поток, произведенный из одной или нескольких углеводородных фракций, полученных во второй системе фракционирования.
13. Способ по п.11, в котором температура кипения углеводородного потока соответствует интервалу кипения атмосферного или вакуумного газойля.
14. Способ по п.11, в котором введение в контакт парового продукта с углеводородным потоком осуществляется в противоточной абсорбционной колонне.
15. Способ повышения качества тяжелого дистиллятного сырья, включающий:
введение в контакт водорода и тяжелого дистиллятного сырья с цеолитным селективным катализатором гидрокрекинга в системе реакторов гидрокрекинга в кипящем слое для получения выходящего потока;
выведение выходящего потока из системы реакторов гидрокрекинга в кипящем слое; и
фракционирование выходящего потока из системы реакторов гидрокрекинга в кипящем слое для получения одной или нескольких углеводородных фракций.
16. Способ по п.15, дополнительно включающий:
введение в контакт углеводородного сырьевого остатка и водорода с металлосодержащим катализатором гидропереработки на нецеолитной основе в первой системе реакторов гидропереработки в кипящем слое для получения первого выходящего потока;
фракционирование первого выходящего потока из первого реактора гидропереработки в кипящем слое для получения первой жидкой фракции и первой паровой фракции;
введение в контакт первой паровой фракции с углеводородным потоком для получения второй паровой фракции и второй жидкой фракции;
введение второй паровой фракции в систему реакторов гидрокрекинга в кипящем слое.
17. Способ по п.15, дополнительно включающий введение в контакт остаточного углеводородного сырья и водорода в реакторе гидропереработки в кипящем слое.
18. Способ по п.15, в котором цеолитный селективный катализатор гидрокрекинга изготавливается таким образом, что он подлежит псевдоожижению и высокое сопротивление истиранию в условиях реакции в реакторе гидрокрекинга в кипящем слое.
19. Способ по п.18, в котором цеолитный селективный катализатор гидрокрекинга содержит благородный металл, нанесенный на цеолитный носитель.
20. Система повышения качества углеводородных остатков и тяжелого дистиллятного сырья, включающая:
первую систему реакторов гидрокрекинга в кипящем слое, содержащих цеолитный селективный катализатор гидрокрекинга для реакции тяжелого дистиллятного сырья и водорода для получения первого выходящего потока;
первый блок фракционирования для фракционирования первого выходящего потока для получения одной или нескольких углеводородных фракций.
21. Система по п.20, дополнительно включающая:
вторую систему реакторов гидропереработки в кипящем слое, содержащих металлосодержащий катализатор гидропереработки на нецеолитной основе для реакции углеводородных остатков и водорода для получения второго выходящего потока;
первый сепаратор для разделения второго выходящего потока и получения жидкой фракции и паровой фракции, причем паровая фракция направляется в первую систему реакторов гидрокрекинга в кипящем слое.
22. Система повышения качества углеводородных остатков и тяжелого дистиллятного сырья, включающая:
первую систему реакторов гидропереработки в кипящем слое, содержащих металлосодержащий катализатор гидропереработки на нецеолитной основе для реакции сырьевого остатка и водорода для получения первого выходящего потока;
первый сепаратор для разделения первого выходящего потока и получения жидкой фракции и паровой фракции;
абсорбционную колонну с использованием углеводородного потока фракции газойля для получения второй паровой фракции и второй жидкой фракции из паровой фракции;
вторую систему реакторов гидрокрекинга в кипящем слое, содержащих цеолитный селективный катализатор гидрокрекинга для реакции для получения второго выходящего потока;
первый блок фракционирования для фракционирования второго выходящего потока для получения одной или нескольких углеводородных фракций.
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Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10265685B2 (en) * | 2015-02-04 | 2019-04-23 | Pc-Cups Ltd. | Metallo-silicate catalyst (MSC) compositions, methods of preparation and methods of use in partial upgrading of hydrocarbon feedstocks |
| CN107779226B (zh) * | 2016-08-29 | 2020-01-10 | 中国石油化工股份有限公司 | 多产低碳烯烃的方法以及用于多产低碳烯烃的系统 |
| US10472579B2 (en) * | 2016-11-21 | 2019-11-12 | Saudi Arabian Oil Company | Process and system for conversion of crude oil to petrochemicals and fuel products integrating vacuum gas oil hydrocracking and steam cracking |
| FI20175815A1 (en) * | 2017-09-14 | 2019-03-15 | Neste Oyj | Vessel fuel composition with low sulfur content and process for its preparation |
| CN108067168A (zh) * | 2017-12-13 | 2018-05-25 | 煤炭科学技术研究院有限公司 | 非均相浆态床加氢裂化装置和方法 |
| US11136512B2 (en) | 2019-12-05 | 2021-10-05 | Saudi Arabian Oil Company | Two-stage hydrocracking unit with intermediate HPNA hydrogenation step |
Family Cites Families (45)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2160163A (en) * | 1934-03-09 | 1939-05-30 | Standard Oil Dev Co | Process for fractionating gaseous mixtures |
| GB966915A (en) * | 1960-11-23 | 1964-08-19 | Hydrocarbon Research Inc | Process for contacting a hydrocarbon liquid with a gas comprising hydrogen |
| US4612108A (en) * | 1985-08-05 | 1986-09-16 | Mobil Oil Corporation | Hydrocracking process using zeolite beta |
| US5108580A (en) | 1989-03-08 | 1992-04-28 | Texaco Inc. | Two catalyst stage hydrocarbon cracking process |
| US5277793A (en) | 1989-05-10 | 1994-01-11 | Chevron Research And Technology Company | Hydrocracking process |
| US5073530A (en) | 1989-05-10 | 1991-12-17 | Chevron Research And Technology Company | Hydrocracking catalyst and process |
| US5069890A (en) | 1989-06-19 | 1991-12-03 | Texaco Inc. | Zeolite treating process |
| US4952306A (en) | 1989-09-22 | 1990-08-28 | Exxon Research And Engineering Company | Slurry hydroprocessing process |
| DE4007543A1 (de) | 1990-03-09 | 1991-09-12 | Veba Oel Technologie Gmbh | Hochdruckheissabscheider |
| US5141909A (en) | 1991-01-22 | 1992-08-25 | Chevron Research And Technology Company | Zeolitic catalyst having selectivity for jet fuel |
| US5340563A (en) | 1992-06-30 | 1994-08-23 | Chevron Research And Technology Company | Preparation of zeolites using low silica/alumina zeolites as a source of aluminum |
| US5866501A (en) | 1996-02-23 | 1999-02-02 | Pradhan; Vivek R. | Dispersed anion-modified iron oxide catalysts for hydroconversion processes |
| WO1998000384A1 (fr) | 1996-06-28 | 1998-01-08 | China Petrochemical Corporation | Procede d'hydrocraquage d'une huile de distillat lourde a des pressions moyennes |
| FR2764902B1 (fr) | 1997-06-24 | 1999-07-16 | Inst Francais Du Petrole | Procede de conversion de fractions lourdes petrolieres comprenant une etape de conversion en lit bouillonnant et une etape d'hydrocraquage |
| US6712955B1 (en) | 1997-07-15 | 2004-03-30 | Exxonmobil Research And Engineering Company | Slurry hydroprocessing using bulk multimetallic catalysts |
| US5935418A (en) | 1997-08-29 | 1999-08-10 | Exxon Research And Engineering Co. | Slurry hydroprocessing |
| JP4248142B2 (ja) | 1997-11-03 | 2009-04-02 | エクソンモービル オイル コーポレイション | 低圧ナフサ水素化分解プロセス |
| FR2791354B1 (fr) | 1999-03-25 | 2003-06-13 | Inst Francais Du Petrole | Procede de conversion de fractions lourdes petrolieres comprenant une etape d'hydroconversion en lits bouillonnants et une etape d'hydrotraitement |
| US6239321B1 (en) * | 2000-02-28 | 2001-05-29 | Bp Amoco Corporation | Upgrading light oligomers |
| US6514403B1 (en) | 2000-04-20 | 2003-02-04 | Abb Lummus Global Inc. | Hydrocracking of vacuum gas and other oils using a cocurrent/countercurrent reaction system and a post-treatment reactive distillation system |
| US6547956B1 (en) | 2000-04-20 | 2003-04-15 | Abb Lummus Global Inc. | Hydrocracking of vacuum gas and other oils using a post-treatment reactive distillation system |
| US7238276B2 (en) | 2000-05-19 | 2007-07-03 | China Petroleum Corporation | Medium-pressure hydrocracking process |
| US6726832B1 (en) * | 2000-08-15 | 2004-04-27 | Abb Lummus Global Inc. | Multiple stage catalyst bed hydrocracking with interstage feeds |
| US6454932B1 (en) | 2000-08-15 | 2002-09-24 | Abb Lummus Global Inc. | Multiple stage ebullating bed hydrocracking with interstage stripping and separating |
| CN1098337C (zh) | 2000-11-02 | 2003-01-08 | 中国石油天然气股份有限公司 | 一种采用多金属液体催化剂的常压重油悬浮床加氢新工艺 |
| US6436279B1 (en) * | 2000-11-08 | 2002-08-20 | Axens North America, Inc. | Simplified ebullated-bed process with enhanced reactor kinetics |
| JP4773634B2 (ja) * | 2001-06-08 | 2011-09-14 | 日本ケッチェン株式会社 | 重質炭化水素油の２段階水素化処理方法 |
| US6860986B2 (en) | 2002-11-08 | 2005-03-01 | Chevron U.S.A. Inc. | Extremely low acidity ultrastable Y zeolite catalyst composition and process |
| US7238277B2 (en) | 2004-12-16 | 2007-07-03 | Chevron U.S.A. Inc. | High conversion hydroprocessing |
| EP1830959B1 (fr) * | 2004-12-23 | 2011-07-06 | Institut Français du Pétrole | Catalyseur zeolithique a teneur controlee en element dopant et procede ameliore de traitement de charges hydrocarbonees |
| US7713407B2 (en) | 2006-06-02 | 2010-05-11 | Exxonmobil Research & Engineering Company | Production of low sulfur fuels using improved hydrocracker post-treatment catalyst |
| ITMI20071198A1 (it) | 2007-06-14 | 2008-12-15 | Eni Spa | Procedimento migliorato per l'idroconversione di oli pesanti con sistemi a letto ebullato |
| US7938952B2 (en) * | 2008-05-20 | 2011-05-10 | Institute Francais Du Petrole | Process for multistage residue hydroconversion integrated with straight-run and conversion gasoils hydroconversion steps |
| US8025793B2 (en) | 2008-06-30 | 2011-09-27 | Uop Llc | Process for using catalyst with rapid formation of iron sulfide in slurry hydrocracking |
| US8062505B2 (en) | 2008-06-30 | 2011-11-22 | Uop Llc | Process for using iron oxide and alumina catalyst with large particle diameter for slurry hydrocracking |
| US8128810B2 (en) | 2008-06-30 | 2012-03-06 | Uop Llc | Process for using catalyst with nanometer crystallites in slurry hydrocracking |
| US7820135B2 (en) | 2008-06-30 | 2010-10-26 | Uop Llc | Catalyst composition with nanometer crystallites for slurry hydrocracking |
| US8066867B2 (en) | 2008-11-10 | 2011-11-29 | Uop Llc | Combination of mild hydrotreating and hydrocracking for making low sulfur diesel and high octane naphtha |
| US8110090B2 (en) | 2009-03-25 | 2012-02-07 | Uop Llc | Deasphalting of gas oil from slurry hydrocracking |
| US8287720B2 (en) * | 2009-06-23 | 2012-10-16 | Lummus Technology Inc. | Multistage resid hydrocracking |
| 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 |
| US8343334B2 (en) | 2009-10-06 | 2013-01-01 | Saudi Arabian Oil Company | Pressure cascaded two-stage hydrocracking unit |
| FR2951193B1 (fr) | 2009-10-13 | 2011-12-09 | Inst Francais Du Petrole | Procede d'hydrocraquage mettant en oeuvre une zeolithe modifiee |
| CA2854335A1 (en) | 2011-11-04 | 2013-05-10 | Saudi Arabian Oil Company | Hydrocracking process with integral intermediate hydrogen separation and purification |
| US20140034549A1 (en) | 2012-08-03 | 2014-02-06 | Lummus Technology Inc. | Residue hydrocracking |
-
2014
- 2014-02-12 US US14/179,083 patent/US10208261B2/en active Active
-
2015
- 2015-02-03 BR BR112016016710-4A patent/BR112016016710B1/pt active IP Right Grant
- 2015-02-03 PT PT157488198T patent/PT3105305T/pt unknown
- 2015-02-03 KR KR1020167016810A patent/KR101899699B1/ko active IP Right Grant
- 2015-02-03 ES ES15748819T patent/ES2748682T3/es active Active
- 2015-02-03 WO PCT/US2015/014235 patent/WO2015123052A1/en active Application Filing
- 2015-02-03 SG SG11201606703XA patent/SG11201606703XA/en unknown
- 2015-02-03 CN CN201580007004.5A patent/CN105980532B/zh active Active
- 2015-02-03 EP EP15748819.8A patent/EP3105305B1/en active Active
- 2015-02-03 HU HUE15748819A patent/HUE045621T2/hu unknown
- 2015-02-03 CA CA2931241A patent/CA2931241C/en active Active
- 2015-02-03 MY MYPI2016000848A patent/MY174114A/en unknown
- 2015-02-03 MX MX2016010102A patent/MX2016010102A/es unknown
- 2015-02-03 RS RS20191308A patent/RS59510B1/sr unknown
- 2015-02-03 RU RU2016136357A patent/RU2654478C2/ru active
- 2015-02-03 PL PL15748819T patent/PL3105305T3/pl unknown
- 2015-02-12 TW TW104104821A patent/TWI558806B/zh active
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2019
- 2019-01-31 US US16/263,956 patent/US10894922B2/en active Active
- 2019-10-04 HR HRP20191810TT patent/HRP20191810T1/hr unknown
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| Publication number | Publication date |
|---|---|
| US20190249095A1 (en) | 2019-08-15 |
| HUE045621T2 (hu) | 2020-01-28 |
| US10894922B2 (en) | 2021-01-19 |
| BR112016016710B1 (pt) | 2021-01-05 |
| TW201536911A (zh) | 2015-10-01 |
| WO2015123052A1 (en) | 2015-08-20 |
| KR101899699B1 (ko) | 2018-10-04 |
| RU2016136357A3 (ru) | 2018-03-15 |
| HRP20191810T1 (hr) | 2019-12-27 |
| PT3105305T (pt) | 2019-10-18 |
| BR112016016710A2 (pt) | 2018-05-08 |
| ES2748682T3 (es) | 2020-03-17 |
| US20150225657A1 (en) | 2015-08-13 |
| US10208261B2 (en) | 2019-02-19 |
| EP3105305B1 (en) | 2019-07-10 |
| CA2931241A1 (en) | 2015-08-20 |
| RS59510B1 (sr) | 2019-12-31 |
| KR20160090353A (ko) | 2016-07-29 |
| MX2016010102A (es) | 2016-10-07 |
| MY174114A (en) | 2020-03-10 |
| CN105980532A (zh) | 2016-09-28 |
| SG11201606703XA (en) | 2016-09-29 |
| CA2931241C (en) | 2019-01-15 |
| RU2654478C2 (ru) | 2018-05-21 |
| EP3105305A4 (en) | 2017-10-25 |
| CN105980532B (zh) | 2018-01-19 |
| TWI558806B (zh) | 2016-11-21 |
| PL3105305T3 (pl) | 2020-01-31 |
| EP3105305A1 (en) | 2016-12-21 |
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