BR112017017299A2 - método de hidrotatamento para produto de síntese de fischer-trosch de baixa temperatura - Google Patents
método de hidrotatamento para produto de síntese de fischer-trosch de baixa temperaturaInfo
- Publication number
- BR112017017299A2 BR112017017299A2 BR112017017299A BR112017017299A BR112017017299A2 BR 112017017299 A2 BR112017017299 A2 BR 112017017299A2 BR 112017017299 A BR112017017299 A BR 112017017299A BR 112017017299 A BR112017017299 A BR 112017017299A BR 112017017299 A2 BR112017017299 A2 BR 112017017299A2
- Authority
- BR
- Brazil
- Prior art keywords
- reaction region
- reaction
- catalyst
- diesel oil
- fischer
- 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
- 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
-
- 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
- B01J21/12—Silica and 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/882—Molybdenum and cobalt
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/88—Molybdenum
- B01J23/883—Molybdenum and nickel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- 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
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8913—Cobalt and noble metals
-
- 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
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/892—Nickel and noble 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
- C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
- C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
- C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1022—Fischer-Tropsch products
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
- C10G2300/1048—Middle distillates
- C10G2300/1055—Diesel having a boiling range of about 230 - 330 °C
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
trata-se de um método de hidrotatamento para um produto de síntese de fischer-trosch de baixa temperatura da presente invenção que compreende as seguintes etapas de: (1) primeiramente, misturar uma cera de fischer-tropsch com um catalisador líquido que contém enxofre em uma certa proporção, então, colocar os mesmos em contato com gás de hidrogênio, então, primeiramente alimentar os mesmos em uma primeira região de reação de um catalisador de pré-tratamento de hidrogenação e, então, alimentar o efluente da primeira região de reação em uma segunda região de reação preenchida com um catalisador de hidrocraqueamento e realizar uma reação de hidrocraqueamento; (2) alimentar um produto do hidrocraqueamento da segunda região de reação, em conjunto com uma nafta e um óleo de diesel de fischer-tropsch, em uma terceira região de reação de modo a entrar em contato com um catalisador de hidrorrefinação, e realizar uma reação de hidrorrefinação; então, alimentar o efluente da reação de hidrorrefinação em uma quarta região de reação de modo a entrar em contato com um catalisador de redução do ponto de fluidez de hidroisomerização, e realizar uma reação de redução do ponto de fluidez de isomerização; e (3) alimentar o efluente da quarta região de reação em um sistema de separação gás-líquido c, em que um gás rico em hidrogênio é separado do mesmo e reciclado, e um produto líquido é alimentado em um sistema de fracionamento d e separado de modo a obter nafta, óleo diesel e um óleo residual, em que o óleo residual é circulado de volta à segunda região de reação. por meio da presente invenção, a densidade do óleo diesel sintetizado pode ser aumentada, o ponto de condensação pode ser diminuído, e os índices para um óleo diesel automotivo podem ser alcançados.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510071747.0A CN104611056B (zh) | 2015-02-11 | 2015-02-11 | 一种低温费托合成产物的加氢处理方法 |
| PCT/CN2016/073024 WO2016127840A1 (zh) | 2015-02-11 | 2016-02-01 | 一种低温费托合成产物的加氢处理方法 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BR112017017299A2 true BR112017017299A2 (pt) | 2018-04-10 |
Family
ID=53145710
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BR112017017299A BR112017017299A2 (pt) | 2015-02-11 | 2016-02-01 | método de hidrotatamento para produto de síntese de fischer-trosch de baixa temperatura |
Country Status (10)
| Country | Link |
|---|---|
| US (1) | US10227537B2 (pt) |
| EP (1) | EP3257918A4 (pt) |
| JP (1) | JP6501897B2 (pt) |
| KR (1) | KR101987436B1 (pt) |
| CN (1) | CN104611056B (pt) |
| AU (1) | AU2016218804B2 (pt) |
| BR (1) | BR112017017299A2 (pt) |
| CA (1) | CA2976291A1 (pt) |
| RU (1) | RU2650190C1 (pt) |
| WO (1) | WO2016127840A1 (pt) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104611056B (zh) * | 2015-02-11 | 2017-03-08 | 武汉凯迪工程技术研究总院有限公司 | 一种低温费托合成产物的加氢处理方法 |
| CN105148909B (zh) * | 2015-08-31 | 2017-11-28 | 上海纳克润滑技术有限公司 | 一种用于烃类加氢裂化的负载型催化剂及其制备和使用方法 |
| CN105778995B (zh) * | 2016-04-18 | 2018-03-20 | 武汉凯迪工程技术研究总院有限公司 | 低温费托合成油与劣质原料油联合加氢生产优质柴油的方法及其设备 |
| CN109988629B (zh) | 2017-12-29 | 2021-08-31 | 中国石油化工股份有限公司 | 一种蜡油加氢裂化方法和系统 |
| CN111659462B (zh) * | 2020-06-30 | 2023-10-27 | 中化泉州石化有限公司 | 一种高活性异构降凝催化剂的制备方法 |
| CN113908817B (zh) * | 2020-07-09 | 2024-04-09 | 国家能源投资集团有限责任公司 | 催化剂用载体及其制备方法、降凝催化剂及其制备方法与应用 |
| CN114437791B (zh) * | 2020-10-19 | 2023-03-10 | 中国石油化工股份有限公司 | 费托合成油低压、长周期加氢裂化工艺 |
| CN114437788B (zh) * | 2020-10-19 | 2023-09-01 | 中国石油化工股份有限公司 | 一种费托合成油加工工艺 |
| CN115612523B (zh) * | 2021-07-13 | 2023-10-20 | 国家能源投资集团有限责任公司 | 费托合成的加氢裂化原料的精制方法、精制加氢裂化原料 |
| CN116042270A (zh) * | 2021-10-28 | 2023-05-02 | 中国石油化工股份有限公司 | 一种生产重石脑油和喷气燃料的加氢裂化方法 |
| CN116064082A (zh) * | 2021-10-29 | 2023-05-05 | 中国石油化工股份有限公司 | 一种多产低凝柴油的两段加氢裂化方法 |
| CN116060110A (zh) * | 2021-10-29 | 2023-05-05 | 中国石油化工股份有限公司 | 一种费托合成蜡加氢裂化催化剂及其制备方法 |
| CN116120966A (zh) * | 2021-11-15 | 2023-05-16 | 中国科学院大连化学物理研究所 | 一种宽馏程费托合成蜡加氢转化的方法 |
| CN116262882A (zh) * | 2021-12-13 | 2023-06-16 | 中国石油化工股份有限公司 | 一种生产石脑油、轻质乙烯料和优质尾油的加氢裂化方法 |
Family Cites Families (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4943672A (en) * | 1987-12-18 | 1990-07-24 | Exxon Research And Engineering Company | Process for the hydroisomerization of Fischer-Tropsch wax to produce lubricating oil (OP-3403) |
| US5378348A (en) * | 1993-07-22 | 1995-01-03 | Exxon Research And Engineering Company | Distillate fuel production from Fischer-Tropsch wax |
| US6656342B2 (en) * | 2001-04-04 | 2003-12-02 | Chevron U.S.A. Inc. | Graded catalyst bed for split-feed hydrocracking/hydrotreating |
| US6515034B2 (en) * | 2001-05-11 | 2003-02-04 | Chevron U.S.A. Inc. | Co-hydroprocessing of Fischer-Tropsch products and crude oil fractions |
| FR2826972B1 (fr) * | 2001-07-06 | 2007-03-23 | Inst Francais Du Petrole | Procede de production de distillats moyens par hydroisomerisation et hydrocraquage d'une fraction lourde issue d'un effluent produit par le procede fischer-tropsch |
| US20030221990A1 (en) * | 2002-06-04 | 2003-12-04 | Yoon H. Alex | Multi-stage hydrocracker with kerosene recycle |
| US20040159582A1 (en) * | 2003-02-18 | 2004-08-19 | Simmons Christopher A. | Process for producing premium fischer-tropsch diesel and lube base oils |
| 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 |
| US20070062847A1 (en) * | 2005-09-16 | 2007-03-22 | Hyde Evan P | Integrated lubricant upgrading process using once-through, hydrogen-containing treat gas |
| CN101210198B (zh) * | 2006-12-27 | 2012-03-21 | 中国石油化工股份有限公司 | 一种生产优质柴油和优质重整原料的加氢方法 |
| CN101230291B (zh) * | 2007-01-23 | 2012-02-29 | 中国石油化工股份有限公司 | 一种低能耗的费托合成产物的加工方法 |
| CN101177625B (zh) * | 2007-04-11 | 2011-12-07 | 中科合成油技术有限公司 | 费-托合成油的加氢处理工艺 |
| CN101177619A (zh) * | 2007-04-13 | 2008-05-14 | 中科合成油技术有限公司 | 由费-托合成蜡生产柴油和化工原料的方法 |
| US8597502B2 (en) * | 2007-09-28 | 2013-12-03 | Japan Oil, Gas And Metals National Corporation | Method of manufacturing diesel fuel base stock and diesel fuel base stock thereof |
| FR2926087B1 (fr) * | 2008-01-04 | 2010-02-12 | Inst Francais Du Petrole | Procede multietapes de production de distillats moyens par hydroisomerisation et hydrocraquage d'un effluent produit par le procede fischer-tropsch |
| CN104611056B (zh) * | 2015-02-11 | 2017-03-08 | 武汉凯迪工程技术研究总院有限公司 | 一种低温费托合成产物的加氢处理方法 |
-
2015
- 2015-02-11 CN CN201510071747.0A patent/CN104611056B/zh active Active
-
2016
- 2016-02-01 RU RU2017131517A patent/RU2650190C1/ru not_active IP Right Cessation
- 2016-02-01 AU AU2016218804A patent/AU2016218804B2/en not_active Ceased
- 2016-02-01 WO PCT/CN2016/073024 patent/WO2016127840A1/zh active Application Filing
- 2016-02-01 EP EP16748641.4A patent/EP3257918A4/en not_active Withdrawn
- 2016-02-01 JP JP2017541755A patent/JP6501897B2/ja active Active
- 2016-02-01 CA CA2976291A patent/CA2976291A1/en not_active Abandoned
- 2016-02-01 BR BR112017017299A patent/BR112017017299A2/pt not_active IP Right Cessation
- 2016-02-01 KR KR1020177025570A patent/KR101987436B1/ko active IP Right Grant
-
2017
- 2017-08-10 US US15/673,439 patent/US10227537B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN104611056B (zh) | 2017-03-08 |
| AU2016218804A1 (en) | 2017-09-28 |
| EP3257918A4 (en) | 2018-08-22 |
| RU2650190C1 (ru) | 2018-04-11 |
| AU2016218804B2 (en) | 2019-04-04 |
| CN104611056A (zh) | 2015-05-13 |
| KR20170118131A (ko) | 2017-10-24 |
| US10227537B2 (en) | 2019-03-12 |
| WO2016127840A1 (zh) | 2016-08-18 |
| CA2976291A1 (en) | 2016-08-18 |
| KR101987436B1 (ko) | 2019-06-10 |
| JP6501897B2 (ja) | 2019-04-17 |
| EP3257918A1 (en) | 2017-12-20 |
| US20170335208A1 (en) | 2017-11-23 |
| JP2018508624A (ja) | 2018-03-29 |
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