CA2290685A1 - Benzene conversion in an improved gasoline upgrading process - Google Patents
Benzene conversion in an improved gasoline upgrading process Download PDFInfo
- Publication number
- CA2290685A1 CA2290685A1 CA002290685A CA2290685A CA2290685A1 CA 2290685 A1 CA2290685 A1 CA 2290685A1 CA 002290685 A CA002290685 A CA 002290685A CA 2290685 A CA2290685 A CA 2290685A CA 2290685 A1 CA2290685 A1 CA 2290685A1
- Authority
- CA
- Canada
- Prior art keywords
- feed
- olefins
- benzene
- hydrodesulfurization
- naphtha
- 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.)
- Granted
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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/04—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of catalytic cracking 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/20—Organic compounds not containing metal atoms
- C10G29/205—Organic compounds not containing metal atoms by reaction with hydrocarbons added to the hydrocarbon oil
-
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
- C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
- C10G47/12—Inorganic carriers
- C10G47/16—Crystalline alumino-silicate carriers
-
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
- C10G69/12—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step
- C10G69/123—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step alkylation
Abstract
Low sulfur gasoline is produced from an olefinic, cracked, sulfur-containing naphtha by treatment over an acidic catalyst, preferably an intermediate pore size zeolite such as ZSM-5 to crack low octane paraffins and olefins under mild conditions with limited aromatization of olefins and naphthenes. A benzene-rich co-feed is co-processed with the naphtha to reduce the benzene levels in teh co-feed by alkylation. This initial processing step is followed by hydrodesulfurization over a hydrotreating catalyst such as CoMo on alumina. In addition to reducing benzene levels in the combined feeds, the initial treatment over the acidic catalyst removes the olefins which would otherwise be saturated in the hydrodesulfurization, consuming hydrogen and lowering product octane, and converts them to compounds which make a positive contribution to octave. Overall liquid yield is high, typically at least 90 % or higher. Product aromatics are typically increased by no more than 25 wt.% relative to the combined feeds and may be lower than the feed.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/862,229 US5865987A (en) | 1995-07-07 | 1997-05-23 | Benzene conversion in an improved gasoline upgrading process |
US08/862,229 | 1997-05-23 | ||
PCT/US1998/009581 WO1998053029A1 (en) | 1997-05-23 | 1998-05-12 | Benzene conversion in an improved gasoline upgrading process |
Publications (2)
Publication Number | Publication Date |
---|---|
CA2290685A1 true CA2290685A1 (en) | 1998-11-26 |
CA2290685C CA2290685C (en) | 2008-07-22 |
Family
ID=25337992
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002290685A Expired - Fee Related CA2290685C (en) | 1997-05-23 | 1998-05-12 | Benzene conversion in an improved gasoline upgrading process |
Country Status (15)
Country | Link |
---|---|
US (1) | US5865987A (en) |
EP (1) | EP0988356B1 (en) |
KR (1) | KR100532160B1 (en) |
CN (1) | CN1298815C (en) |
AR (1) | AR012735A1 (en) |
AT (1) | ATE270319T1 (en) |
BR (1) | BR9809454A (en) |
CA (1) | CA2290685C (en) |
CZ (1) | CZ299503B6 (en) |
DE (1) | DE69824850T2 (en) |
ES (1) | ES2219887T3 (en) |
PL (1) | PL190882B1 (en) |
PT (1) | PT988356E (en) |
RU (1) | RU2186831C2 (en) |
WO (1) | WO1998053029A1 (en) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6602403B1 (en) | 1998-05-05 | 2003-08-05 | Exxonmobil Chemical Patents Inc. | Process for selectively producing high octane naphtha |
US6803494B1 (en) | 1998-05-05 | 2004-10-12 | Exxonmobil Chemical Patents Inc. | Process for selectively producing propylene in a fluid catalytic cracking process |
US6455750B1 (en) * | 1998-05-05 | 2002-09-24 | Exxonmobil Chemical Patents Inc. | Process for selectively producing light olefins |
US6106697A (en) | 1998-05-05 | 2000-08-22 | Exxon Research And Engineering Company | Two stage fluid catalytic cracking process for selectively producing b. C.su2 to C4 olefins |
US6388152B1 (en) | 1998-05-05 | 2002-05-14 | Exxonmobil Chemical Patents Inc. | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
US6339180B1 (en) | 1998-05-05 | 2002-01-15 | Exxonmobil Chemical Patents, Inc. | Process for producing polypropylene from C3 olefins selectively produced in a fluid catalytic cracking process |
US6315890B1 (en) | 1998-05-05 | 2001-11-13 | Exxonmobil Chemical Patents Inc. | Naphtha cracking and hydroprocessing process for low emissions, high octane fuels |
US6313366B1 (en) | 1998-05-05 | 2001-11-06 | Exxonmobile Chemical Patents, Inc. | Process for selectively producing C3 olefins in a fluid catalytic cracking process |
US6118035A (en) | 1998-05-05 | 2000-09-12 | Exxon Research And Engineering Co. | Process for selectively producing light olefins in a fluid catalytic cracking process from a naphtha/steam feed |
AT4070U3 (en) * | 1999-11-12 | 2001-07-25 | Rosinger Anlagentechnik Gmbh & | FERMENTATION REACTOR WITH TIP SAFETY REGARDING BIOLOGY |
US6599417B2 (en) * | 2000-01-21 | 2003-07-29 | Bp Corporation North America Inc. | Sulfur removal process |
US6602405B2 (en) * | 2000-01-21 | 2003-08-05 | Bp Corporation North America Inc. | Sulfur removal process |
US7837861B2 (en) * | 2006-10-18 | 2010-11-23 | Exxonmobil Research & Engineering Co. | Process for benzene reduction and sulfur removal from FCC naphthas |
KR101475977B1 (en) * | 2007-09-07 | 2014-12-23 | 제이엑스 닛코닛세키에너지주식회사 | Solid acid, process for producing the solid acid, method for desulfurizing hydrocarbon oil using solid acid as desulfurizing agent |
WO2017081595A1 (en) | 2015-11-12 | 2017-05-18 | Sabic Global Technologies B.V. | Methods for producing aromatics and olefins |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3957625A (en) * | 1975-02-07 | 1976-05-18 | Mobil Oil Corporation | Method for reducing the sulfur level of gasoline product |
US4784745A (en) * | 1987-05-18 | 1988-11-15 | Mobil Oil Corporation | Catalytic upgrading of FCC effluent |
US4827069A (en) * | 1988-02-19 | 1989-05-02 | Mobil Oil Corporation | Upgrading light olefin fuel gas and catalytic reformate in a turbulent fluidized bed catalyst reactor |
US4950387A (en) * | 1988-10-21 | 1990-08-21 | Mobil Oil Corp. | Upgrading of cracking gasoline |
US4992607A (en) * | 1989-03-20 | 1991-02-12 | Mobil Oil Corporation | Petroleum refinery process and apparatus for the production of alkyl aromatic hydrocarbons from fuel gas and catalytic reformate |
EP0420326B1 (en) * | 1989-09-26 | 1995-02-15 | Shell Internationale Researchmaatschappij B.V. | Process for upgrading a sulphur-containing feedstock |
GB8926555D0 (en) * | 1989-11-24 | 1990-01-17 | Shell Int Research | Process for upgrading a sulphur-containing feedstock |
US5510016A (en) * | 1991-08-15 | 1996-04-23 | Mobil Oil Corporation | Gasoline upgrading process |
US5326463A (en) * | 1991-08-15 | 1994-07-05 | Mobil Oil Corporation | Gasoline upgrading process |
US5391288A (en) * | 1991-08-15 | 1995-02-21 | Mobil Oil Corporation | Gasoline upgrading process |
US5346609A (en) * | 1991-08-15 | 1994-09-13 | Mobil Oil Corporation | Hydrocarbon upgrading process |
US5409596A (en) * | 1991-08-15 | 1995-04-25 | Mobil Oil Corporation | Hydrocarbon upgrading process |
US5414172A (en) * | 1993-03-08 | 1995-05-09 | Mobil Oil Corporation | Naphtha upgrading |
US5347061A (en) * | 1993-03-08 | 1994-09-13 | Mobil Oil Corporation | Process for producing gasoline having lower benzene content and distillation end point |
ES2144049T3 (en) * | 1993-03-08 | 2000-06-01 | Mobil Oil Corp | REDUCTION OF BENZENE IN GASOLINE THROUGH RENTING WITH SUPERIOR OLEFINS. |
JP2001523277A (en) * | 1996-04-09 | 2001-11-20 | シェブロン ユー.エス.エー.インコーポレイテッド | Reverse order operation of a hydroprocessing reactor system. |
-
1997
- 1997-05-23 US US08/862,229 patent/US5865987A/en not_active Expired - Fee Related
-
1998
- 1998-05-12 BR BR9809454-8A patent/BR9809454A/en not_active Application Discontinuation
- 1998-05-12 EP EP98920370A patent/EP0988356B1/en not_active Expired - Lifetime
- 1998-05-12 WO PCT/US1998/009581 patent/WO1998053029A1/en active IP Right Grant
- 1998-05-12 ES ES98920370T patent/ES2219887T3/en not_active Expired - Lifetime
- 1998-05-12 AT AT98920370T patent/ATE270319T1/en not_active IP Right Cessation
- 1998-05-12 PL PL336999A patent/PL190882B1/en not_active IP Right Cessation
- 1998-05-12 CN CNB988072394A patent/CN1298815C/en not_active Expired - Fee Related
- 1998-05-12 PT PT98920370T patent/PT988356E/en unknown
- 1998-05-12 RU RU99127336/04A patent/RU2186831C2/en not_active IP Right Cessation
- 1998-05-12 DE DE69824850T patent/DE69824850T2/en not_active Expired - Fee Related
- 1998-05-12 KR KR10-1999-7010671A patent/KR100532160B1/en not_active IP Right Cessation
- 1998-05-12 CZ CZ0414399A patent/CZ299503B6/en not_active IP Right Cessation
- 1998-05-12 CA CA002290685A patent/CA2290685C/en not_active Expired - Fee Related
- 1998-05-21 AR ARP980102370A patent/AR012735A1/en unknown
Also Published As
Publication number | Publication date |
---|---|
CN1264416A (en) | 2000-08-23 |
EP0988356B1 (en) | 2004-06-30 |
AR012735A1 (en) | 2000-11-08 |
DE69824850T2 (en) | 2004-11-04 |
KR20010012710A (en) | 2001-02-26 |
CA2290685C (en) | 2008-07-22 |
WO1998053029A1 (en) | 1998-11-26 |
CN1298815C (en) | 2007-02-07 |
US5865987A (en) | 1999-02-02 |
PL336999A1 (en) | 2000-07-31 |
CZ299503B6 (en) | 2008-08-20 |
ATE270319T1 (en) | 2004-07-15 |
PT988356E (en) | 2004-09-30 |
EP0988356A1 (en) | 2000-03-29 |
PL190882B1 (en) | 2006-02-28 |
EP0988356A4 (en) | 2002-08-21 |
DE69824850D1 (en) | 2004-08-05 |
CZ414399A3 (en) | 2000-06-14 |
RU2186831C2 (en) | 2002-08-10 |
BR9809454A (en) | 2000-06-20 |
KR100532160B1 (en) | 2005-11-30 |
ES2219887T3 (en) | 2004-12-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EEER | Examination request | ||
MKLA | Lapsed |