AR036570A1 - Proceso y sistema para hidroprocesar una carga de hidrocarburo - Google Patents
Proceso y sistema para hidroprocesar una carga de hidrocarburoInfo
- Publication number
- AR036570A1 AR036570A1 ARP020103566A ARP020103566A AR036570A1 AR 036570 A1 AR036570 A1 AR 036570A1 AR P020103566 A ARP020103566 A AR P020103566A AR P020103566 A ARP020103566 A AR P020103566A AR 036570 A1 AR036570 A1 AR 036570A1
- Authority
- AR
- Argentina
- Prior art keywords
- catalyst
- hydroprocessing
- hydrocarbon
- hydrogen
- containing gas
- 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
- C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
Abstract
Un proceso para hidroprocesar una carga de hidrocarburo con un caudal conocido de gas que contiene hidrógeno y un volumen de catalizador, que incluye las etapas de proveer una carga de hidrocarburo que tiene una característica inicial; alimentar dicha carga de hidrocarburo y una primera porción de dicho gas que contiene hidrógeno en corriente conjunta a una zona de hidroprocesamiento que contiene una primera porción de dicho catalizador de modo de proveer un primer producto de hidrocarburo; proveer una zona de hidroprocesamiento adicional que contiene un resto de dicho catalizador; alimentar dicho primer producto de hidrocarburo en corriente conjunta con un resto de dicho gas que contiene hidrógeno a dicha zona de hidroprocesamiento de modo de proveer un producto de hidrocarburo final que tenga una característica final mejorada en comparación con dicha característica inicial, donde dicha primera porción de dicho gas que contiene hidrógeno está comprendida aproximadamente entre 30 y 80% en volumen de dicho caudal conocido de dicho gas que contiene hidrógeno, y dicha primera porción de dicho catalizador está comprendida aproximadamente entre 30 y 70% en peso de dicho volumen de catalizador. Se describe también un sistema para hidroprocesar la carga de hidrocarburo.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/960,442 US6656348B2 (en) | 2001-03-01 | 2001-09-24 | Hydroprocessing process |
Publications (1)
Publication Number | Publication Date |
---|---|
AR036570A1 true AR036570A1 (es) | 2004-09-15 |
Family
ID=25503158
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP020103566A AR036570A1 (es) | 2001-09-24 | 2002-09-20 | Proceso y sistema para hidroprocesar una carga de hidrocarburo |
Country Status (10)
Country | Link |
---|---|
US (2) | US6656348B2 (es) |
EP (1) | EP1295932B1 (es) |
AR (1) | AR036570A1 (es) |
AT (1) | ATE360674T1 (es) |
BR (1) | BR0203830A (es) |
DE (1) | DE60219736T2 (es) |
ES (1) | ES2284760T3 (es) |
MX (1) | MX240745B (es) |
NL (1) | NL1021504C2 (es) |
NO (1) | NO20024423L (es) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7166209B2 (en) | 2001-03-01 | 2007-01-23 | Intevep, S.A. | Hydroprocessing process |
US20070286837A1 (en) * | 2006-05-17 | 2007-12-13 | Torgerson Peter M | Hair care composition comprising an aminosilicone and a high viscosity silicone copolymer emulsion |
CN101376840B (zh) * | 2007-08-27 | 2011-10-12 | 中国石油化工股份有限公司 | 重质馏分油加氢处理方法 |
US7731838B2 (en) * | 2007-09-11 | 2010-06-08 | Exxonmobil Research And Engineering Company | Solid acid assisted deep desulfurization of diesel boiling range feeds |
US8747653B2 (en) | 2011-03-31 | 2014-06-10 | Uop Llc | Process for hydroprocessing two streams |
US8158070B1 (en) | 2011-03-31 | 2012-04-17 | Uop Llc | Apparatus for hydroprocessing two streams |
US8608940B2 (en) | 2011-03-31 | 2013-12-17 | Uop Llc | Process for mild hydrocracking |
US8158069B1 (en) | 2011-03-31 | 2012-04-17 | Uop Llc | Apparatus for mild hydrocracking |
US8753501B2 (en) | 2011-10-21 | 2014-06-17 | Uop Llc | Process and apparatus for producing diesel |
US8518351B2 (en) | 2011-03-31 | 2013-08-27 | Uop Llc | Apparatus for producing diesel |
US8696885B2 (en) | 2011-03-31 | 2014-04-15 | Uop Llc | Process for producing diesel |
US8691078B2 (en) | 2011-05-17 | 2014-04-08 | Uop Llc | Process for hydroprocessing hydrocarbons |
US11788017B2 (en) | 2017-02-12 | 2023-10-17 | Magëmã Technology LLC | Multi-stage process and device for reducing environmental contaminants in heavy marine fuel oil |
US10655074B2 (en) | 2017-02-12 | 2020-05-19 | Mag{hacek over (e)}m{hacek over (a)} Technology LLC | Multi-stage process and device for reducing environmental contaminates in heavy marine fuel oil |
US10604709B2 (en) | 2017-02-12 | 2020-03-31 | Magēmā Technology LLC | Multi-stage device and process for production of a low sulfur heavy marine fuel oil from distressed heavy fuel oil materials |
Family Cites Families (34)
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US3119765A (en) * | 1959-10-19 | 1964-01-28 | Exxon Research Engineering Co | Catalytic treatment of crude oils |
US3519557A (en) * | 1969-08-15 | 1970-07-07 | Sun Oil Co | Controlled hydrogenation process |
US3691152A (en) * | 1971-03-10 | 1972-09-12 | Texaco Inc | Hydrodesulfurization and blending of residue-containing petroleum oil |
US3809664A (en) | 1973-08-16 | 1974-05-07 | Us Agriculture | Method of preparing starch graft polymers |
US3876530A (en) * | 1973-08-22 | 1975-04-08 | Gulf Research Development Co | Multiple stage hydrodesulfurization with greater sulfur and metal removal in initial stage |
US3860511A (en) * | 1974-01-22 | 1975-01-14 | Gulf Research Development Co | Two-stage residual oil hydrodesulfurication process with ammonia addition |
US3967936A (en) * | 1975-01-02 | 1976-07-06 | The United States Of America As Represented By The United States Energy Research And Development Administration | Methanation process utilizing split cold gas recycle |
US4016070A (en) | 1975-11-17 | 1977-04-05 | Gulf Research & Development Company | Multiple stage hydrodesulfurization process with extended downstream catalyst life |
JPS595011B2 (ja) * | 1979-11-27 | 1984-02-02 | 千代田化工建設株式会社 | 重質炭化水素油の水素化処理用触媒ならびにその製法 |
US4431525A (en) | 1982-04-26 | 1984-02-14 | Standard Oil Company (Indiana) | Three-catalyst process for the hydrotreating of heavy hydrocarbon streams |
US4877647A (en) | 1986-04-17 | 1989-10-31 | Kansas State University Research Foundation | Method of coating substrates with solvated clusters of metal particles |
GB8910711D0 (en) | 1989-05-10 | 1989-06-28 | Davy Mckee London | Process |
US5110444A (en) | 1990-08-03 | 1992-05-05 | Uop | Multi-stage hydrodesulfurization and hydrogenation process for distillate hydrocarbons |
US5183556A (en) | 1991-03-13 | 1993-02-02 | Abb Lummus Crest Inc. | Production of diesel fuel by hydrogenation of a diesel feed |
US5779992A (en) | 1993-08-18 | 1998-07-14 | Catalysts & Chemicals Industries Co., Ltd. | Process for hydrotreating heavy oil and hydrotreating apparatus |
US5759939A (en) | 1994-04-08 | 1998-06-02 | Kansas State University Research Foundation | Composite metal oxide adsorbents |
EP0793701B1 (en) | 1994-11-25 | 1999-01-27 | Kvaerner Process Technology Limited | Multi-step hydrodesulfurization process |
US6007787A (en) | 1996-08-23 | 1999-12-28 | Exxon Research And Engineering Co. | Countercurrent reaction vessel |
US5985131A (en) | 1996-08-23 | 1999-11-16 | Exxon Research And Engineering Company | Hydroprocessing in a countercurrent reaction vessel |
US5939031A (en) | 1996-08-23 | 1999-08-17 | Exxon Research And Engineering Co. | Countercurrent reactor |
US5935420A (en) | 1996-08-23 | 1999-08-10 | Exxon Research And Engineering Co. | Desulfurization process for refractory organosulfur heterocycles |
US5928498A (en) | 1996-08-23 | 1999-07-27 | Exxon Research And Engineering Co. | Desulfurization and ring opening of petroleum streams |
US5925239A (en) | 1996-08-23 | 1999-07-20 | Exxon Research And Engineering Co. | Desulfurization and aromatic saturation of feedstreams containing refractory organosulfur heterocycles and aromatics |
US5705052A (en) | 1996-12-31 | 1998-01-06 | Exxon Research And Engineering Company | Multi-stage hydroprocessing in a single reaction vessel |
US5720872A (en) | 1996-12-31 | 1998-02-24 | Exxon Research And Engineering Company | Multi-stage hydroprocessing with multi-stage stripping in a single stripper vessel |
EP0870817A1 (en) | 1997-04-11 | 1998-10-14 | Akzo Nobel N.V. | Process for effecting deep HDS of hydrocarbon feedstocks |
US6017442A (en) | 1997-09-18 | 2000-01-25 | Phillips Petroleum Company | Hydrocarbon conversion with dual metal promoted zeolite |
US6017443A (en) | 1998-02-05 | 2000-01-25 | Mobil Oil Corporation | Hydroprocessing process having staged reaction zones |
US6054041A (en) * | 1998-05-06 | 2000-04-25 | Exxon Research And Engineering Co. | Three stage cocurrent liquid and vapor hydroprocessing |
US5985136A (en) | 1998-06-18 | 1999-11-16 | Exxon Research And Engineering Co. | Two stage hydrodesulfurization process |
US6087294A (en) | 1998-08-12 | 2000-07-11 | Kansas State University Research Foundation | Dispersion and stabilization of reactive atoms on the surface of metal oxides |
US5968346A (en) | 1998-09-16 | 1999-10-19 | Exxon Research And Engineering Co. | Two stage hydroprocessing with vapor-liquid interstage contacting for vapor heteroatom removal |
US6649042B2 (en) * | 2001-03-01 | 2003-11-18 | Intevep, S.A. | Hydroprocessing process |
US7166209B2 (en) * | 2001-03-01 | 2007-01-23 | Intevep, S.A. | Hydroprocessing process |
-
2001
- 2001-09-24 US US09/960,442 patent/US6656348B2/en not_active Expired - Lifetime
-
2002
- 2002-07-19 US US10/200,266 patent/US7648685B2/en not_active Expired - Fee Related
- 2002-09-16 NO NO20024423A patent/NO20024423L/no not_active Application Discontinuation
- 2002-09-19 BR BR0203830-7A patent/BR0203830A/pt not_active IP Right Cessation
- 2002-09-20 AT AT02021029T patent/ATE360674T1/de not_active IP Right Cessation
- 2002-09-20 NL NL1021504A patent/NL1021504C2/nl not_active IP Right Cessation
- 2002-09-20 DE DE60219736T patent/DE60219736T2/de not_active Revoked
- 2002-09-20 EP EP02021029A patent/EP1295932B1/en not_active Revoked
- 2002-09-20 AR ARP020103566A patent/AR036570A1/es not_active Application Discontinuation
- 2002-09-20 ES ES02021029T patent/ES2284760T3/es not_active Expired - Lifetime
- 2002-09-23 MX MXPA02009292 patent/MX240745B/es active IP Right Grant
Also Published As
Publication number | Publication date |
---|---|
US6656348B2 (en) | 2003-12-02 |
ATE360674T1 (de) | 2007-05-15 |
EP1295932B1 (en) | 2007-04-25 |
DE60219736T2 (de) | 2007-12-27 |
NO20024423L (no) | 2003-03-25 |
DE60219736D1 (de) | 2007-06-06 |
US20030035765A1 (en) | 2003-02-20 |
NO20024423D0 (no) | 2002-09-16 |
NL1021504C2 (nl) | 2003-06-17 |
ES2284760T3 (es) | 2007-11-16 |
US7648685B2 (en) | 2010-01-19 |
NL1021504A1 (nl) | 2003-03-25 |
MX240745B (es) | 2006-10-04 |
EP1295932A1 (en) | 2003-03-26 |
MXPA02009292A (es) | 2004-12-13 |
US20020166796A1 (en) | 2002-11-14 |
BR0203830A (pt) | 2003-06-03 |
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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 |