AR064673A1 - Proceso de conversion de hidrocarburos que incluye un sistema de reaccion con derivacion escalonada - Google Patents
Proceso de conversion de hidrocarburos que incluye un sistema de reaccion con derivacion escalonadaInfo
- Publication number
- AR064673A1 AR064673A1 ARP070105842A ARP070105842A AR064673A1 AR 064673 A1 AR064673 A1 AR 064673A1 AR P070105842 A ARP070105842 A AR P070105842A AR P070105842 A ARP070105842 A AR P070105842A AR 064673 A1 AR064673 A1 AR 064673A1
- Authority
- AR
- Argentina
- Prior art keywords
- hydrocarbon conversion
- reaction system
- reaction
- derivation
- scaled
- 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
- 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
- C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
- C10G69/14—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural parallel stages only
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/10—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed
-
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/16—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "moving bed" method
-
- 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
- C10G35/00—Reforming naphtha
- C10G35/04—Catalytic reforming
- C10G35/10—Catalytic reforming with moving catalysts
- C10G35/12—Catalytic reforming with moving catalysts according to the "moving-bed" method
-
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/002—Apparatus for fixed bed hydrotreatment processes
-
- 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
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/10—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 with moving solid particles
- C10G49/14—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 with moving solid particles according to the "moving-bed" technique
-
- 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
- C10G51/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
- C10G51/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only
- C10G51/026—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural serial stages only only catalytic cracking 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
- C10G59/00—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
- C10G59/02—Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha plural serial stages only
-
- 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
-
- 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
- C10G65/14—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only
- C10G65/18—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural parallel stages only including only cracking 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
Una realizacion ejemplificativa puede incluir un proceso de conversion de hidrocarburos. En general, el proceso incluye pasar un caudal de hidrocarburos por una zona de conversion de hidrocarburos (10) que comprende una serie de zonas de reaccion (12). Típicamente, la zona de conversion de hidrocarburos incluye un sistema de reaccion con derivacion escalonada (30) que posee una primera (150), segunda (200), tercera (250), y cuarta zona de reaccion (300), las cuales son zonas de reaccion con derivacion escalonada, y una quina zona de reaccion (320), que puede ser una zona de reaccion sin derivacion escalonada, luego del sistema de reaccion con derivacion escalonada.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/615,254 US7622620B2 (en) | 2006-12-22 | 2006-12-22 | Hydrocarbon conversion process including a staggered-bypass reaction system |
Publications (1)
Publication Number | Publication Date |
---|---|
AR064673A1 true AR064673A1 (es) | 2009-04-15 |
Family
ID=39543877
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP070105842A AR064673A1 (es) | 2006-12-22 | 2007-12-21 | Proceso de conversion de hidrocarburos que incluye un sistema de reaccion con derivacion escalonada |
Country Status (7)
Country | Link |
---|---|
US (2) | US7622620B2 (es) |
EP (1) | EP2094817A4 (es) |
KR (1) | KR101460378B1 (es) |
AR (1) | AR064673A1 (es) |
MY (1) | MY145888A (es) |
TW (1) | TWI367939B (es) |
WO (1) | WO2008079619A1 (es) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8373014B2 (en) * | 2009-12-17 | 2013-02-12 | Uop Llc | Solid catalyst hydrocarbon alkylation using stacked moving bed radial flow reactors |
US8329028B2 (en) * | 2009-12-17 | 2012-12-11 | Uop Llc | Solid catalyst hydrocarbon conversion process using stacked moving bed reactors |
US9085736B2 (en) * | 2011-10-26 | 2015-07-21 | Chevron Phillips Chemical Company Lp | System and method for on stream catalyst replacement |
US8906223B2 (en) * | 2012-11-20 | 2014-12-09 | Uop Llc | High temperature reforming process for integration into existing units |
US8900442B2 (en) * | 2012-11-20 | 2014-12-02 | Uop Llc | High temperature CCR process with integrated reactor bypasses |
CN105462608B (zh) * | 2014-09-12 | 2017-06-30 | 中国石油化工股份有限公司 | 一种石脑油连续催化重整方法 |
US10436762B2 (en) | 2017-11-07 | 2019-10-08 | Chevron Phillips Chemical Company Lp | System and method for monitoring a reforming catalyst |
Family Cites Families (44)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3853745A (en) | 1973-03-07 | 1974-12-10 | Exxon Research Engineering Co | Low temperature-low pressure naphtha reforming process |
US4022682A (en) * | 1975-12-22 | 1977-05-10 | Gulf Research & Development Company | Hydrodenitrogenation of shale oil using two catalysts in series reactors |
US4119527A (en) | 1977-05-09 | 1978-10-10 | Uop Inc. | Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles |
US4119526A (en) | 1977-05-09 | 1978-10-10 | Uop Inc. | Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles |
US4441988A (en) | 1979-05-30 | 1984-04-10 | Irvine Robert L | Catalytic reformer process |
US4250018A (en) * | 1979-09-06 | 1981-02-10 | Uop Inc. | Multiple stage hydrocarbon conversion process |
US4436612A (en) | 1979-10-09 | 1984-03-13 | Exxon Research And Engineering Co. | Catalytic reforming process |
US4427533A (en) | 1979-10-09 | 1984-01-24 | Exxon Research And Engineering Co. | Catalytic reforming process |
US4354271A (en) * | 1980-04-28 | 1982-10-12 | Rockwell International Corporation | Frequency-controlled, unstable optical resonator |
US4325806A (en) | 1981-01-05 | 1982-04-20 | Uop Inc. | Multiple stage hydrocarbon conversion with gravity flowing catalyst particles |
US4325807A (en) | 1981-01-05 | 1982-04-20 | Uop Inc. | Multiple stage hydrocarbon conversion with gravity flowing catalyst particles |
US4425222A (en) | 1981-06-08 | 1984-01-10 | Exxon Research And Engineering Co. | Catalytic reforming process |
US4348271A (en) | 1981-07-14 | 1982-09-07 | Exxon Research & Engineering Co. | Catalytic reforming process |
US4354925A (en) | 1981-07-30 | 1982-10-19 | Exxon Research And Engineering Co. | Catalytic reforming process |
JPS5871990A (ja) | 1981-10-23 | 1983-04-28 | Nippon Oil Co Ltd | 炭素繊維用原料ピッチの製造方法 |
US4411869A (en) | 1981-12-28 | 1983-10-25 | Uop Inc. | Multiple stage reactor system |
US4411870A (en) | 1981-12-28 | 1983-10-25 | Uop Inc. | Reactor system |
US4440626A (en) | 1981-12-31 | 1984-04-03 | Exxon Research And Engineering Co. | Catalytic reforming process |
CA1223836A (en) | 1981-12-31 | 1987-07-07 | William E. Winter | Catalytic reforming process |
US4406777A (en) | 1982-01-19 | 1983-09-27 | Mobil Oil Corporation | Fixed bed reactor operation |
US4406775A (en) | 1982-02-01 | 1983-09-27 | Exxon Research And Engineering Co. | Catalyst regeneration process |
US4440627A (en) | 1983-03-10 | 1984-04-03 | Exxon Research And Engineering Co. | Catalytic reforming process |
US4789528A (en) | 1983-04-26 | 1988-12-06 | Mobil Oil Corporation | Technique for sequential rotation of reactors in a multi-reactor catalytic conversion system |
US4498973A (en) | 1983-06-17 | 1985-02-12 | Uop Inc. | Multiple-stage catalytic reforming with gravity-flowing dissimilar catalyst particles |
US4567023A (en) | 1984-02-27 | 1986-01-28 | Uop Inc. | Multiple-stage reactor system for a moving catalyst bed |
US4578370A (en) * | 1985-04-25 | 1986-03-25 | Uop Inc. | Gas circulation method for moving bed catalyst regeneration zones |
US4613423A (en) | 1985-05-02 | 1986-09-23 | Exxon Research And Engineering Co. | Catalytic reforming process |
US4599471A (en) * | 1985-09-16 | 1986-07-08 | Uop Inc. | Method for oxygen addition to oxidative reheat zone of hydrocarbon dehydrogenation process |
US4769128A (en) | 1987-06-15 | 1988-09-06 | Exxon Research And Engineering Company | Regeneration and reactivation of reforming catalysts avoiding iron scale carryover from the regenerator circuit to the reactors |
US4764267A (en) | 1987-10-29 | 1988-08-16 | Chevron Research Company | Multi-stage catalytic reforming with high rhenium content catalyst |
US4872967A (en) | 1988-05-23 | 1989-10-10 | Exxon Research And Engineering Company | Multistage reforming with interstage aromatics removal |
US4975178A (en) | 1988-05-23 | 1990-12-04 | Exxon Research & Engineering Company | Multistage reforming with interstage aromatics removal |
US5073250A (en) | 1990-03-02 | 1991-12-17 | Chevron Research & Technology Company | Staged catalyst reforming to produce optimum octane barrel per calendar day reformate production |
US5376259A (en) | 1990-03-02 | 1994-12-27 | Chevron Research And Technology Company | Staged catalyst processing to produce optimum aromatic barrel per calendar day aromatic production |
US5171691A (en) | 1990-03-02 | 1992-12-15 | Chevron Research And Technology Company | Method for controlling multistage reforming process to give high octane barrel per calendar day throughput |
US5407558A (en) | 1990-03-02 | 1995-04-18 | Chevron Research And Technology Company | Method for controlling multistage aromatization process to give high aromatic barrel per calendar day throughput |
US5235121A (en) | 1991-08-02 | 1993-08-10 | Phillips Petroleum Company | Method for reforming hydrocarbons |
US5203988A (en) | 1991-08-19 | 1993-04-20 | Exxon Research & Engineering Company | Multistage reforming with ultra-low pressure cyclic second stage |
US5211838A (en) | 1991-12-09 | 1993-05-18 | Exxon Research & Engineering Company | Fixed-bed/moving-bed two stage catalytic reforming with interstage aromatics removal |
US5779992A (en) * | 1993-08-18 | 1998-07-14 | Catalysts & Chemicals Industries Co., Ltd. | Process for hydrotreating heavy oil and hydrotreating apparatus |
AU4148196A (en) * | 1995-01-13 | 1996-07-31 | Ashland Inc. | Hydrocarbon conversion catalyst additives and processes |
US5879537A (en) | 1996-08-23 | 1999-03-09 | Uop Llc | Hydrocarbon conversion process using staggered bypassing of reaction zones |
US7033488B2 (en) | 2002-10-04 | 2006-04-25 | Conocophillips Company | Method of removing and replacing catalyst in a multi-reactor cascade configuration |
US20050274648A1 (en) | 2004-04-21 | 2005-12-15 | Goldstein Stuart S | Method for revamping fixed-bed catalytic reformers |
-
2006
- 2006-12-22 US US11/615,254 patent/US7622620B2/en active Active
-
2007
- 2007-12-06 WO PCT/US2007/086604 patent/WO2008079619A1/en active Application Filing
- 2007-12-06 KR KR1020097013149A patent/KR101460378B1/ko not_active IP Right Cessation
- 2007-12-06 EP EP07865289.8A patent/EP2094817A4/en not_active Withdrawn
- 2007-12-06 MY MYPI20092487A patent/MY145888A/en unknown
- 2007-12-21 TW TW096149596A patent/TWI367939B/zh not_active IP Right Cessation
- 2007-12-21 AR ARP070105842A patent/AR064673A1/es not_active Application Discontinuation
-
2008
- 2008-10-29 US US12/260,312 patent/US7638664B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
TWI367939B (en) | 2012-07-11 |
US20080154076A1 (en) | 2008-06-26 |
KR101460378B1 (ko) | 2014-11-10 |
MY145888A (en) | 2012-05-15 |
US20090054712A1 (en) | 2009-02-26 |
TW200848501A (en) | 2008-12-16 |
KR20090102762A (ko) | 2009-09-30 |
US7622620B2 (en) | 2009-11-24 |
EP2094817A4 (en) | 2013-05-01 |
US7638664B2 (en) | 2009-12-29 |
WO2008079619A1 (en) | 2008-07-03 |
EP2094817A1 (en) | 2009-09-02 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG | Grant, registration | ||
FD | Application declared void or lapsed, e.g., due to non-payment of fee |