CA2405019C - Production de distillats a faible teneur en soufre - Google Patents
Production de distillats a faible teneur en soufre Download PDFInfo
- Publication number
- CA2405019C CA2405019C CA2405019A CA2405019A CA2405019C CA 2405019 C CA2405019 C CA 2405019C CA 2405019 A CA2405019 A CA 2405019A CA 2405019 A CA2405019 A CA 2405019A CA 2405019 C CA2405019 C CA 2405019C
- Authority
- CA
- Canada
- Prior art keywords
- stage
- hydrodesulfurization
- hydrogen
- stream
- sulfur
- 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.)
- Expired - Lifetime
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
- 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
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)
Abstract
L'invention concerne un procédé d'hydrotraitement d'un écoulement du type distillat visant à produire un écoulement à teneur en soufre exceptionnellement faible, la teneur en aromatiques totaux et polynucléaires étant modérément réduite. A cet effet, on hydrodésulfure un écoulement du type distillat au cours d'une première étape d'hydrodésulfuration. L'écoulement obtenu subit une première étape de séparation donnant lieu à la production d'un écoulement en phase vapeur et d'un écoulement liquide. L'écoulement en phase liquide subit une seconde étape d'hydrodésulfuration, et l'écoulement obtenu passe par une seconde étape de séparation donnant lieu à la production d'un écoulement en phase vapeur et d'un écoulement liquide à faible teneur en soufre. Un partie au moins de l'écoulement en phase vapeur tiré de la seconde étape de séparation peut être réintroduit en cascade au niveau de la première étape d'hydrodésulfuration.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/553,107 US7435335B1 (en) | 1998-12-08 | 2000-04-20 | Production of low sulfur distillates |
US09/553,107 | 2000-04-20 | ||
PCT/US2001/012516 WO2001081506A1 (fr) | 2000-04-20 | 2001-04-17 | Production de distillats a faible teneur en soufre |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2405019A1 CA2405019A1 (fr) | 2001-11-01 |
CA2405019C true CA2405019C (fr) | 2010-06-22 |
Family
ID=24208163
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA2405019A Expired - Lifetime CA2405019C (fr) | 2000-04-20 | 2001-04-17 | Production de distillats a faible teneur en soufre |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP1334166B1 (fr) |
JP (1) | JP5469791B2 (fr) |
AU (2) | AU5165701A (fr) |
CA (1) | CA2405019C (fr) |
NO (1) | NO20025020L (fr) |
WO (1) | WO2001081506A1 (fr) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8632675B2 (en) * | 2008-12-24 | 2014-01-21 | Exxonmobil Research And Engineering Company | Co-processing of diesel biofeed and heavy oil |
DE102011101503A1 (de) * | 2011-05-16 | 2012-11-22 | Schott Ag | Sensorbauteilgehäuse |
US10273420B2 (en) | 2014-10-27 | 2019-04-30 | Uop Llc | Process for hydrotreating a hydrocarbons stream |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8910711D0 (en) * | 1989-05-10 | 1989-06-28 | Davy Mckee London | Process |
JP2530498B2 (ja) * | 1989-08-31 | 1996-09-04 | 東燃株式会社 | 石油蒸留物の低イオウ化方法 |
JP2519191B2 (ja) * | 1990-04-10 | 1996-07-31 | 触媒化成工業株式会社 | 灯軽油の水素化処理方法 |
US5114562A (en) * | 1990-08-03 | 1992-05-19 | Uop | Two-stage hydrodesulfurization and hydrogenation process for distillate hydrocarbons |
JP2921379B2 (ja) * | 1993-12-30 | 1999-07-19 | 株式会社コスモ総合研究所 | 軽油の水素化脱硫方法 |
DK0727474T3 (da) * | 1995-02-14 | 2000-09-04 | Nippon Mitsubishi Oil Corp | Fremgangsmåde til hydrogenering af aromatiske carbonhydrider i barbonhydridolie og katalysator til anvendelse i denne fremg |
JP3634041B2 (ja) * | 1995-12-26 | 2005-03-30 | 財団法人石油産業活性化センター | 軽油の高品質化処理法 |
US6231753B1 (en) * | 1996-02-02 | 2001-05-15 | Exxon Research And Engineering Company | Two stage deep naphtha desulfurization with reduced mercaptan formation |
FR2757532B1 (fr) * | 1996-12-20 | 1999-02-19 | Inst Francais Du Petrole | Procede de transformation d'une coupe gazole pour produire un carburant a haute indice de cetane, desaromatise et desulfure |
JP4050364B2 (ja) * | 1997-09-11 | 2008-02-20 | 日揮株式会社 | 石油の処理方法および石油の処理装置 |
US6103104A (en) * | 1998-05-07 | 2000-08-15 | Exxon Research And Engineering Company | Multi-stage hydroprocessing of middle distillates to avoid color bodies |
JP4282118B2 (ja) * | 1998-10-05 | 2009-06-17 | 新日本石油株式会社 | 軽油の水素化脱硫方法 |
AU756565B2 (en) * | 1998-12-08 | 2003-01-16 | Exxonmobil Research And Engineering Company | Production of low sulfur/low aromatics distillates |
-
2001
- 2001-04-17 CA CA2405019A patent/CA2405019C/fr not_active Expired - Lifetime
- 2001-04-17 JP JP2001578580A patent/JP5469791B2/ja not_active Expired - Fee Related
- 2001-04-17 AU AU5165701A patent/AU5165701A/xx active Pending
- 2001-04-17 EP EP01925059.6A patent/EP1334166B1/fr not_active Expired - Lifetime
- 2001-04-17 WO PCT/US2001/012516 patent/WO2001081506A1/fr active Application Filing
- 2001-04-17 AU AU2001251657A patent/AU2001251657B2/en not_active Expired
-
2002
- 2002-10-18 NO NO20025020A patent/NO20025020L/no not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
EP1334166B1 (fr) | 2017-11-29 |
JP2003531274A (ja) | 2003-10-21 |
EP1334166A4 (fr) | 2004-10-20 |
AU5165701A (en) | 2001-11-07 |
JP5469791B2 (ja) | 2014-04-16 |
NO20025020L (no) | 2002-12-19 |
EP1334166A1 (fr) | 2003-08-13 |
WO2001081506A1 (fr) | 2001-11-01 |
AU2001251657B2 (en) | 2006-05-18 |
CA2405019A1 (fr) | 2001-11-01 |
NO20025020D0 (no) | 2002-10-18 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKEX | Expiry |
Effective date: 20210419 |