MXPA05012731A - Hidrogenacion del destilado intermedio usando un reactor a contra-corriente. - Google Patents
Hidrogenacion del destilado intermedio usando un reactor a contra-corriente.Info
- Publication number
- MXPA05012731A MXPA05012731A MXPA05012731A MXPA05012731A MXPA05012731A MX PA05012731 A MXPA05012731 A MX PA05012731A MX PA05012731 A MXPA05012731 A MX PA05012731A MX PA05012731 A MXPA05012731 A MX PA05012731A MX PA05012731 A MXPA05012731 A MX PA05012731A
- Authority
- MX
- Mexico
- Prior art keywords
- hydrogenation
- reaction zone
- hydrogen
- counter
- hydrocarbon feed
- 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
- 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
- C10G65/02—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
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
-
- 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
- C10G65/08—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a hydrogenation of the aromatic hydrocarbons
-
- 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
- C10G2300/1048—Middle distillates
-
- 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
- C10G2300/1048—Middle distillates
- C10G2300/1055—Diesel having a boiling range of about 230 - 330 °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
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
-
- 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
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV
-
- 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
- C10G2400/04—Diesel oil
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Un proceso para la hidrogenacion de una alimentacion de hidrocarburos incluye poner en contacto una cantidad principal de la alimentacion de hidrocarburos con hidrogeno de una manera a contra-corriente en una primera zona de reaccion bajo condiciones de reaccion de hidrogenacion en la presencia de un catalizador de hidrogenacion en al menos un primer lecho de catalizador, en donde existe un efluente liquido en un extremo del fondo de la primera zona de reaccion y existe un efluente gaseoso que contiene hidrogeno en un extremo superior de la primera zona de reaccion, y poner en contacto una porcion menor de la alimentacion de hidrocarburos con dicho efluente gaseoso que contiene hidrogeno de una manera a co-corriente en una segunda zona de reaccion que tiene un lecho de catalizador posicionado para recibir el efluente que contiene hidrogeno de la primera zona de reaccion.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/449,046 US7247235B2 (en) | 2003-05-30 | 2003-05-30 | Hydrogenation of middle distillate using a counter-current reactor |
PCT/US2004/016910 WO2004108637A2 (en) | 2003-05-30 | 2004-05-28 | Hydrogenation of middle distillate using a counter-current reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
MXPA05012731A true MXPA05012731A (es) | 2006-02-22 |
Family
ID=33451678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
MXPA05012731A MXPA05012731A (es) | 2003-05-30 | 2004-05-28 | Hidrogenacion del destilado intermedio usando un reactor a contra-corriente. |
Country Status (11)
Country | Link |
---|---|
US (1) | US7247235B2 (es) |
EP (4) | EP2295523A3 (es) |
JP (2) | JP5124141B2 (es) |
CN (2) | CN100540635C (es) |
BR (1) | BRPI0410819B1 (es) |
CA (1) | CA2526659C (es) |
MX (1) | MXPA05012731A (es) |
RU (1) | RU2304609C2 (es) |
UA (1) | UA88261C2 (es) |
WO (1) | WO2004108637A2 (es) |
ZA (1) | ZA200509685B (es) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7247235B2 (en) * | 2003-05-30 | 2007-07-24 | Abb Lummus Global Inc, | Hydrogenation of middle distillate using a counter-current reactor |
US7419586B2 (en) * | 2004-12-27 | 2008-09-02 | Exxonmobil Research And Engineering Company | Two-stage hydrodesulfurization of cracked naphtha streams with light naphtha bypass or removal |
US20070289900A1 (en) * | 2006-06-14 | 2007-12-20 | Alvarez Walter E | Hydrogenation of polynuclear aromatic compounds |
US20080159928A1 (en) * | 2006-12-29 | 2008-07-03 | Peter Kokayeff | Hydrocarbon Conversion Process |
FR2923490B1 (fr) * | 2007-11-12 | 2009-12-18 | Inst Francais Du Petrole | Procede d'hydroconversion de charges lourdes en lit bouillonnant avec injection de la charge en tete de reacteur |
US8020838B2 (en) * | 2009-03-31 | 2011-09-20 | Uop Llc | Contacting stages for co-current contacting apparatuses |
US8424181B2 (en) * | 2009-04-17 | 2013-04-23 | Exxonmobil Research And Engineering Company | High pressure revamp of low pressure distillate hydrotreating process units |
WO2011061576A1 (en) * | 2009-11-20 | 2011-05-26 | Total Raffinage Marketing | Process for the production of hydrocarbon fluids having a low aromatic content |
CN102311759B (zh) * | 2010-07-07 | 2015-02-18 | 中国石油化工股份有限公司 | 一种柴油加氢脱硫方法 |
WO2012134836A2 (en) * | 2011-03-31 | 2012-10-04 | Uop Llc | Process and apparatus for hydroprocessing two streams |
CN104011181B (zh) * | 2011-11-04 | 2017-02-15 | 沙特阿拉伯石油公司 | 具有集成中间氢分离和纯化的加氢处理和芳烃饱和方法 |
CN103773474B (zh) * | 2012-10-24 | 2016-03-30 | 中国石油化工股份有限公司 | 一种气相、液相混合加氢工艺方法 |
FR3013722B1 (fr) * | 2013-11-28 | 2015-12-04 | Ifp Energies Now | Procede d'hydrotraitement d'un gazole dans des reacteurs en serie avec recyclage d'hydrogene. |
US10273420B2 (en) | 2014-10-27 | 2019-04-30 | Uop Llc | Process for hydrotreating a hydrocarbons stream |
CN106701173B (zh) * | 2015-11-18 | 2018-08-10 | 中国石油天然气股份有限公司 | 液相加氢装置及方法 |
CN106701179B (zh) * | 2015-11-18 | 2018-09-04 | 中国石油天然气股份有限公司 | 液相加氢装置及方法 |
CN106701180B (zh) * | 2015-11-18 | 2018-09-04 | 中国石油天然气股份有限公司 | 液相加氢装置及方法 |
JP7147760B2 (ja) * | 2017-07-04 | 2022-10-05 | 三菱ケミカル株式会社 | 芳香族炭化水素の製造方法 |
US12018218B2 (en) | 2018-05-25 | 2024-06-25 | Shell Usa, Inc. | Hydrocracking process for making middle distillate from a light hydrocarbon feedstock |
CN112142551B (zh) * | 2020-09-08 | 2023-06-16 | 德州中科易工工程技术有限公司 | 一种铜基催化剂催化乙炔氢氯化合成氯乙烯的装置及方法 |
Family Cites Families (26)
Publication number | Priority date | Publication date | Assignee | Title |
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US3846278A (en) * | 1971-09-02 | 1974-11-05 | Lummus Co | Production of jet fuel |
US3767562A (en) * | 1971-09-02 | 1973-10-23 | Lummus Co | Production of jet fuel |
US3761399A (en) * | 1971-12-08 | 1973-09-25 | Gulf Research Development Co | Two zone hydrodesulfurization of asphaltic fuel oil |
US4021330A (en) * | 1975-09-08 | 1977-05-03 | Continental Oil Company | Hydrotreating a high sulfur, aromatic liquid hydrocarbon |
JPS57123290A (en) * | 1981-01-25 | 1982-07-31 | Chiyoda Chem Eng & Constr Co Ltd | Method for converting heavy hydrocarbon oil into light fractions |
US4576709A (en) * | 1982-09-02 | 1986-03-18 | Ashland Oil, Inc. | Catalytic upgrading of reduced crudes and residual oils with a coke selective catalyst |
US5183556A (en) * | 1991-03-13 | 1993-02-02 | Abb Lummus Crest Inc. | Production of diesel fuel by hydrogenation of a diesel feed |
US5522983A (en) * | 1992-02-06 | 1996-06-04 | Chevron Research And Technology Company | Hydrocarbon hydroconversion process |
US5643442A (en) * | 1994-07-19 | 1997-07-01 | Exxon Research And Engineering Company | Membrane process for enhanced distillate or hydrotreated distillate aromatics reduction |
US5730860A (en) * | 1995-08-14 | 1998-03-24 | The Pritchard Corporation | Process for desulfurizing gasoline and hydrocarbon feedstocks |
US5942197A (en) * | 1996-08-23 | 1999-08-24 | Exxon Research And Engineering Co | Countercurrent reactor |
US6153086A (en) * | 1996-08-23 | 2000-11-28 | Exxon Research And Engineering Company | Combination cocurrent and countercurrent staged hydroprocessing with a vapor stage |
US20010001450A1 (en) | 1996-08-23 | 2001-05-24 | Gerald E. Markley | Multi-stage countercurrent hydrotreating process |
US6495029B1 (en) | 1997-08-22 | 2002-12-17 | Exxon Research And Engineering Company | Countercurrent desulfurization process for refractory organosulfur heterocycles |
US6623621B1 (en) | 1998-12-07 | 2003-09-23 | Exxonmobil Research And Engineering Company | Control of flooding in a countercurrent flow reactor by use of temperature of liquid product stream |
WO2000034416A1 (en) | 1998-12-08 | 2000-06-15 | Exxon Research And Engineering Company | Production of low sulfur/low aromatics distillates |
US6241876B1 (en) * | 1998-12-30 | 2001-06-05 | Mobil Oil Corporation | Selective ring opening process for producing diesel fuel with increased cetane number |
FR2795420B1 (fr) | 1999-06-25 | 2001-08-03 | Inst Francais Du Petrole | Procede d'hydrotraitement d'un distillat moyen dans deux zones successives comprenant une zone intermediaire de stripage de l'effluent de la premiere zone avec condensation des produits lourds sortant en tete du strippeur |
US6312586B1 (en) * | 1999-09-27 | 2001-11-06 | Uop Llc | Multireactor parallel flow hydrocracking process |
US6589416B2 (en) | 2000-07-21 | 2003-07-08 | Exxonmobil Research And Engineering Company | Method and catalyst for opening naphthenic rings of naphthenic ring-containing compounds |
US6402940B1 (en) | 2000-09-01 | 2002-06-11 | Unipure Corporation | Process for removing low amounts of organic sulfur from hydrocarbon fuels |
US6623622B2 (en) | 2000-10-10 | 2003-09-23 | Exxonmobil Research And Engineering Company | Two stage diesel fuel hydrotreating and stripping in a single reaction vessel |
US6444116B1 (en) | 2000-10-10 | 2002-09-03 | Intevep, S.A. | Process scheme for sequentially hydrotreating-hydrocracking diesel and vacuum gas oil |
CN1133721C (zh) * | 2001-01-05 | 2004-01-07 | 中国石油化工集团公司 | 一种烃类加氢处理工艺 |
US6444118B1 (en) * | 2001-02-16 | 2002-09-03 | Catalytic Distillation Technologies | Process for sulfur reduction in naphtha streams |
US7247235B2 (en) * | 2003-05-30 | 2007-07-24 | Abb Lummus Global Inc, | Hydrogenation of middle distillate using a counter-current reactor |
-
2003
- 2003-05-30 US US10/449,046 patent/US7247235B2/en not_active Expired - Lifetime
-
2004
- 2004-05-28 EP EP10012480A patent/EP2295523A3/en not_active Withdrawn
- 2004-05-28 MX MXPA05012731A patent/MXPA05012731A/es active IP Right Grant
- 2004-05-28 RU RU2005141451/04A patent/RU2304609C2/ru active
- 2004-05-28 UA UAA200511337A patent/UA88261C2/ru unknown
- 2004-05-28 BR BRPI0410819-1A patent/BRPI0410819B1/pt not_active IP Right Cessation
- 2004-05-28 EP EP10012484A patent/EP2295524A3/en not_active Withdrawn
- 2004-05-28 EP EP04753693A patent/EP1644464A2/en not_active Withdrawn
- 2004-05-28 CN CNB2004800150342A patent/CN100540635C/zh not_active Expired - Fee Related
- 2004-05-28 CN CN200810095418.XA patent/CN101412927B/zh not_active Expired - Fee Related
- 2004-05-28 WO PCT/US2004/016910 patent/WO2004108637A2/en active Application Filing
- 2004-05-28 CA CA2526659A patent/CA2526659C/en not_active Expired - Fee Related
- 2004-05-28 EP EP10012485A patent/EP2295525A3/en not_active Withdrawn
- 2004-05-28 JP JP2006533493A patent/JP5124141B2/ja not_active Expired - Fee Related
-
2005
- 2005-11-30 ZA ZA200509685A patent/ZA200509685B/en unknown
-
2012
- 2012-07-26 JP JP2012165921A patent/JP5572185B2/ja not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP5572185B2 (ja) | 2014-08-13 |
CN101412927B (zh) | 2015-05-20 |
CA2526659A1 (en) | 2004-12-16 |
ZA200509685B (en) | 2006-10-25 |
CN100540635C (zh) | 2009-09-16 |
BRPI0410819A (pt) | 2006-06-27 |
EP2295524A2 (en) | 2011-03-16 |
US20040238409A1 (en) | 2004-12-02 |
EP2295525A3 (en) | 2012-05-02 |
UA88261C2 (ru) | 2009-10-12 |
RU2005141451A (ru) | 2006-06-10 |
CN1798824A (zh) | 2006-07-05 |
EP1644464A2 (en) | 2006-04-12 |
CN101412927A (zh) | 2009-04-22 |
EP2295523A2 (en) | 2011-03-16 |
WO2004108637A2 (en) | 2004-12-16 |
CA2526659C (en) | 2013-07-16 |
JP2007502906A (ja) | 2007-02-15 |
EP2295523A3 (en) | 2012-05-02 |
BRPI0410819B1 (pt) | 2015-04-14 |
JP2012246492A (ja) | 2012-12-13 |
EP2295525A2 (en) | 2011-03-16 |
US7247235B2 (en) | 2007-07-24 |
KR20060054183A (ko) | 2006-05-22 |
JP5124141B2 (ja) | 2013-01-23 |
WO2004108637A3 (en) | 2005-04-14 |
EP2295524A3 (en) | 2012-05-02 |
RU2304609C2 (ru) | 2007-08-20 |
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Legal Events
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FG | Grant or registration |