CA3049804A1 - Desulfuration d'une alimentation d'intervalle de distillation de naphta - Google Patents
Desulfuration d'une alimentation d'intervalle de distillation de naphta Download PDFInfo
- Publication number
- CA3049804A1 CA3049804A1 CA3049804A CA3049804A CA3049804A1 CA 3049804 A1 CA3049804 A1 CA 3049804A1 CA 3049804 A CA3049804 A CA 3049804A CA 3049804 A CA3049804 A CA 3049804A CA 3049804 A1 CA3049804 A1 CA 3049804A1
- Authority
- CA
- Canada
- Prior art keywords
- naphtha
- boiling range
- naphtha boiling
- silicon
- effluent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
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
- 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
- C10G25/00—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
- C10G25/003—Specific sorbent material, not covered by C10G25/02 or C10G25/03
-
- 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
- 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
-
- 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
- C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °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
- 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
- C10G2300/207—Acid gases, e.g. H2S, COS, SO2, HCN
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/308—Gravity, density, e.g. API
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
L'invention concerne des procédés de désulfuration d'une charge d'alimentation de naphta de craqueur catalytique fluide (FCC), des charges d'alimentation de naphta de distillation directe et des combinaisons de ceux-ci. Une charge d'intervalle de distillation de naphta est amenée à passer sur un piège à silicium avant d'être hydrodésulfurée lors d'un procédé catalytique d'hydrodésulfuration de naphta à rétention d'oléfine. L'invention concerne également des procédés d'élimination de silicium de la charge d'alimentation de naphta de FCC, de la charge d'alimentation de naphta de distillation directe et des combinaisons de ceux-ci.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201762461270P | 2017-02-21 | 2017-02-21 | |
US62/461,270 | 2017-02-21 | ||
PCT/US2018/015129 WO2018156294A1 (fr) | 2017-02-21 | 2018-01-25 | Désulfuration d'une alimentation d'intervalle de distillation de naphta |
Publications (1)
Publication Number | Publication Date |
---|---|
CA3049804A1 true CA3049804A1 (fr) | 2018-08-30 |
Family
ID=61189547
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA3049804A Abandoned CA3049804A1 (fr) | 2017-02-21 | 2018-01-25 | Desulfuration d'une alimentation d'intervalle de distillation de naphta |
Country Status (5)
Country | Link |
---|---|
US (1) | US20180237706A1 (fr) |
EP (1) | EP3585866A1 (fr) |
CA (1) | CA3049804A1 (fr) |
SG (1) | SG11201906393TA (fr) |
WO (1) | WO2018156294A1 (fr) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3117892A1 (fr) | 2020-12-21 | 2022-06-24 | IFP Energies Nouvelles | Masse de captation de silicium |
FR3117893A1 (fr) | 2020-12-21 | 2022-06-24 | IFP Energies Nouvelles | Procede de rejuvenation de masse de captation de silicium |
FR3117887A1 (fr) | 2020-12-21 | 2022-06-24 | IFP Energies Nouvelles | Procede de captation de silicium a faible vitesse spatiale horaire |
WO2023170700A1 (fr) | 2022-03-11 | 2023-09-14 | Hindustan Petroleum Corporation Limited | Catalyseur d'hydrotraitement de naphta et son procédé de préparation |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4131537A (en) | 1977-10-04 | 1978-12-26 | Exxon Research & Engineering Co. | Naphtha hydrofining process |
US4243519A (en) | 1979-02-14 | 1981-01-06 | Exxon Research & Engineering Co. | Hydrorefining process |
US4645587A (en) * | 1984-12-07 | 1987-02-24 | Union Oil Company Of California | Process for removing silicon compounds from hydrocarbon streams |
JP3387700B2 (ja) | 1995-07-26 | 2003-03-17 | 新日本石油株式会社 | 接触分解ガソリンの脱硫方法 |
JP3378416B2 (ja) | 1995-08-25 | 2003-02-17 | 新日本石油株式会社 | 接触分解ガソリンの脱硫方法 |
US6409913B1 (en) | 1996-02-02 | 2002-06-25 | Exxonmobil Research And Engineering Company | Naphtha desulfurization with reduced mercaptan formation |
US6013598A (en) | 1996-02-02 | 2000-01-11 | Exxon Research And Engineering Co. | Selective hydrodesulfurization catalyst |
US6231753B1 (en) | 1996-02-02 | 2001-05-15 | Exxon Research And Engineering Company | Two stage deep naphtha desulfurization with reduced mercaptan formation |
US6231754B1 (en) | 1996-02-02 | 2001-05-15 | Exxon Research And Engineering Company | High temperature naphtha desulfurization using a low metal and partially deactivated catalyst |
US5985136A (en) | 1998-06-18 | 1999-11-16 | Exxon Research And Engineering Co. | Two stage hydrodesulfurization process |
US6387249B1 (en) | 1999-12-22 | 2002-05-14 | Exxonmobil Research And Engineering Company | High temperature depressurization for naphtha mercaptan removal |
US6596157B2 (en) | 2000-04-04 | 2003-07-22 | Exxonmobil Research And Engineering Company | Staged hydrotreating method for naphtha desulfurization |
US6913688B2 (en) | 2001-11-30 | 2005-07-05 | Exxonmobil Research And Engineering Company | Multi-stage hydrodesulfurization of cracked naphtha streams with interstage fractionation |
US7297251B2 (en) | 2002-05-21 | 2007-11-20 | Exxonmobil Research And Engineering Company | Multi-stage hydrodesulfurization of cracked naphtha streams with a stacked bed reactor |
US20070114156A1 (en) | 2005-11-23 | 2007-05-24 | Greeley John P | Selective naphtha hydrodesulfurization with high temperature mercaptan decomposition |
US7837861B2 (en) | 2006-10-18 | 2010-11-23 | Exxonmobil Research & Engineering Co. | Process for benzene reduction and sulfur removal from FCC naphthas |
FR2907348B1 (fr) * | 2006-10-18 | 2008-12-12 | Inst Francais Du Petrole | Utilisation d'alumines comme masse de captation de complexes organometalliques du silicium |
WO2014099349A1 (fr) | 2012-12-21 | 2014-06-26 | Exxonmobil Research And Engineering Company | Élimination de mercaptans au moyen de microréacteurs |
US20160046881A1 (en) * | 2014-08-13 | 2016-02-18 | Exxonmobil Research And Engineering Company | Desulfurization of naphtha blends |
-
2018
- 2018-01-25 CA CA3049804A patent/CA3049804A1/fr not_active Abandoned
- 2018-01-25 EP EP18704364.1A patent/EP3585866A1/fr not_active Withdrawn
- 2018-01-25 US US15/879,505 patent/US20180237706A1/en not_active Abandoned
- 2018-01-25 WO PCT/US2018/015129 patent/WO2018156294A1/fr unknown
- 2018-01-25 SG SG11201906393TA patent/SG11201906393TA/en unknown
Also Published As
Publication number | Publication date |
---|---|
WO2018156294A1 (fr) | 2018-08-30 |
SG11201906393TA (en) | 2019-09-27 |
US20180237706A1 (en) | 2018-08-23 |
EP3585866A1 (fr) | 2020-01-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1349905B1 (fr) | Méthode pour la formation d'un naphta à faible teneur en soufre et indice d'octane élevé pour mélange d'essence | |
CA3049804A1 (fr) | Desulfuration d'une alimentation d'intervalle de distillation de naphta | |
US7297251B2 (en) | Multi-stage hydrodesulfurization of cracked naphtha streams with a stacked bed reactor | |
JP4423037B2 (ja) | 段間分留を伴う分解ナフサ流の多段水素化脱硫 | |
US7220352B2 (en) | Selective hydrodesulfurization of naphtha streams | |
JP2004010893A (ja) | 第8族元素およびタングステンを含む触媒の存在下に、硫黄化合物およびオレフィンを含む留分を水素化脱硫するための方法 | |
EP1682636B1 (fr) | Retrait d'azote de flux d'alimentation de naphta olefinique pour ameliorer l'hydrodesulfurisation par rapport a la selectivite de saturation d'olefine | |
JP2014145009A (ja) | 水素化処理方法 | |
US20160046881A1 (en) | Desulfurization of naphtha blends | |
JP6548223B2 (ja) | 燃料油基材の製造方法 | |
JP2012197350A (ja) | 重質油の水素化精製方法 | |
EP1686166A1 (fr) | Composition d'essence sans plomb et procede de production associe | |
AU2009356146B2 (en) | Process for removing arsenic with a trap catalyst before desulfurizating it | |
JP2003027070A (ja) | 分解ガソリン留分の脱硫方法 | |
AU2004261970A1 (en) | A catalyst system and its use in manufacturing low sulfur fuels |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FZDE | Discontinued |
Effective date: 20220726 |
|
FZDE | Discontinued |
Effective date: 20220726 |