AR012735A1 - Un proceso para la hidrosulfuracion de una carga combinada que comprende fracciones que contienen azufre, olefinas y benceno, y para la reduccion delcontenido de benceno de la carga - Google Patents
Un proceso para la hidrosulfuracion de una carga combinada que comprende fracciones que contienen azufre, olefinas y benceno, y para la reduccion delcontenido de benceno de la cargaInfo
- Publication number
- AR012735A1 AR012735A1 ARP980102370A ARP980102370A AR012735A1 AR 012735 A1 AR012735 A1 AR 012735A1 AR P980102370 A ARP980102370 A AR P980102370A AR P980102370 A ARP980102370 A AR P980102370A AR 012735 A1 AR012735 A1 AR 012735A1
- Authority
- AR
- Argentina
- Prior art keywords
- benzene
- reduction
- load
- fractions containing
- containing sulfur
- 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
- 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
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)
- Crystallography & Structural Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Un proceso para la hidrosulfuracion de una carga combinada que comprende fracciones que contienen azufre, olefinas y benceno, y para la reduccion delcontenido de benceno de la carga, que comprende poner en contacto dicha carga, en una primera etapa, bajo condiciones de craqueo suaves con un catalizadorácido solido que consiste en una zeolita ZSM-5 de tamano poral intermedio y actividad ácida, para formar un producto intermedio de contenido reducido debenceno con relacion a la carga combinada; y en una segunda etapa poner en contacto el producto intermedio con un catalizador de hidrodesulfuracion a altapresion, alta temperatura y en presencia de hidrogeno, para convertir y producir un producto desulfurado.
Applications Claiming Priority (1)
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 |
Publications (1)
Publication Number | Publication Date |
---|---|
AR012735A1 true AR012735A1 (es) | 2000-11-08 |
Family
ID=25337992
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP980102370A AR012735A1 (es) | 1997-05-23 | 1998-05-21 | Un proceso para la hidrosulfuracion de una carga combinada que comprende fracciones que contienen azufre, olefinas y benceno, y para la reduccion delcontenido de benceno de la carga |
Country Status (15)
Country | Link |
---|---|
US (1) | US5865987A (es) |
EP (1) | EP0988356B1 (es) |
KR (1) | KR100532160B1 (es) |
CN (1) | CN1298815C (es) |
AR (1) | AR012735A1 (es) |
AT (1) | ATE270319T1 (es) |
BR (1) | BR9809454A (es) |
CA (1) | CA2290685C (es) |
CZ (1) | CZ299503B6 (es) |
DE (1) | DE69824850T2 (es) |
ES (1) | ES2219887T3 (es) |
PL (1) | PL190882B1 (es) |
PT (1) | PT988356E (es) |
RU (1) | RU2186831C2 (es) |
WO (1) | WO1998053029A1 (es) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6455750B1 (en) | 1998-05-05 | 2002-09-24 | Exxonmobil Chemical Patents Inc. | Process for selectively producing light olefins |
US6803494B1 (en) | 1998-05-05 | 2004-10-12 | Exxonmobil Chemical Patents Inc. | Process for selectively producing propylene in a fluid catalytic cracking process |
US6313366B1 (en) | 1998-05-05 | 2001-11-06 | Exxonmobile Chemical Patents, Inc. | Process for selectively producing C3 olefins 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 |
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 |
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 |
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 |
US6602403B1 (en) | 1998-05-05 | 2003-08-05 | Exxonmobil Chemical Patents Inc. | Process for selectively producing high octane naphtha |
AT4070U3 (de) * | 1999-11-12 | 2001-07-25 | Rosinger Anlagentechnik Gmbh & | Fermentationsreaktor mit kippsicherheit bezüglich der biologie |
US6602405B2 (en) * | 2000-01-21 | 2003-08-05 | Bp Corporation North America Inc. | Sulfur removal process |
US6599417B2 (en) * | 2000-01-21 | 2003-07-29 | 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 |
JP5328655B2 (ja) * | 2007-09-07 | 2013-10-30 | Jx日鉱日石エネルギー株式会社 | 固体酸、その製造方法及び固体酸を脱硫剤として用いる炭化水素油の脱硫方法 |
CN108349853B (zh) | 2015-11-12 | 2022-03-15 | 沙特基础工业全球技术公司 | 生产芳烃和烯烃的方法 |
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 |
US5326463A (en) * | 1991-08-15 | 1994-07-05 | Mobil Oil Corporation | Gasoline upgrading process |
US5510016A (en) * | 1991-08-15 | 1996-04-23 | Mobil Oil Corporation | Gasoline upgrading process |
US5409596A (en) * | 1991-08-15 | 1995-04-25 | Mobil Oil Corporation | Hydrocarbon 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 |
US5414172A (en) * | 1993-03-08 | 1995-05-09 | Mobil Oil Corporation | Naphtha upgrading |
DE69423881T2 (de) * | 1993-03-08 | 2000-12-07 | Mobil Oil Corp., Fairfax | Benzolreduktion in benzin durch alkylierung mit höheren olefinen |
US5347061A (en) * | 1993-03-08 | 1994-09-13 | Mobil Oil Corporation | Process for producing gasoline having lower benzene content and distillation end point |
SK166197A3 (en) * | 1996-04-09 | 1998-04-08 | Chevron Usa Inc | Process for reverse staging in hydroprocessing reactor systems |
-
1997
- 1997-05-23 US US08/862,229 patent/US5865987A/en not_active Expired - Fee Related
-
1998
- 1998-05-12 RU RU99127336/04A patent/RU2186831C2/ru not_active IP Right Cessation
- 1998-05-12 WO PCT/US1998/009581 patent/WO1998053029A1/en active IP Right Grant
- 1998-05-12 CZ CZ0414399A patent/CZ299503B6/cs not_active IP Right Cessation
- 1998-05-12 ES ES98920370T patent/ES2219887T3/es not_active Expired - Lifetime
- 1998-05-12 PT PT98920370T patent/PT988356E/pt unknown
- 1998-05-12 AT AT98920370T patent/ATE270319T1/de not_active IP Right Cessation
- 1998-05-12 EP EP98920370A patent/EP0988356B1/en not_active Expired - Lifetime
- 1998-05-12 PL PL336999A patent/PL190882B1/pl not_active IP Right Cessation
- 1998-05-12 CN CNB988072394A patent/CN1298815C/zh not_active Expired - Fee Related
- 1998-05-12 KR KR10-1999-7010671A patent/KR100532160B1/ko not_active IP Right Cessation
- 1998-05-12 DE DE69824850T patent/DE69824850T2/de not_active Expired - Fee Related
- 1998-05-12 BR BR9809454-8A patent/BR9809454A/pt not_active Application Discontinuation
- 1998-05-12 CA CA002290685A patent/CA2290685C/en not_active Expired - Fee Related
- 1998-05-21 AR ARP980102370A patent/AR012735A1/es unknown
Also Published As
Publication number | Publication date |
---|---|
ATE270319T1 (de) | 2004-07-15 |
CZ299503B6 (cs) | 2008-08-20 |
CA2290685A1 (en) | 1998-11-26 |
WO1998053029A1 (en) | 1998-11-26 |
PL190882B1 (pl) | 2006-02-28 |
CN1298815C (zh) | 2007-02-07 |
DE69824850D1 (de) | 2004-08-05 |
RU2186831C2 (ru) | 2002-08-10 |
KR100532160B1 (ko) | 2005-11-30 |
DE69824850T2 (de) | 2004-11-04 |
BR9809454A (pt) | 2000-06-20 |
EP0988356A4 (en) | 2002-08-21 |
PT988356E (pt) | 2004-09-30 |
ES2219887T3 (es) | 2004-12-01 |
CA2290685C (en) | 2008-07-22 |
US5865987A (en) | 1999-02-02 |
CN1264416A (zh) | 2000-08-23 |
EP0988356A1 (en) | 2000-03-29 |
CZ414399A3 (cs) | 2000-06-14 |
EP0988356B1 (en) | 2004-06-30 |
KR20010012710A (ko) | 2001-02-26 |
PL336999A1 (en) | 2000-07-31 |
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