ES2055548T3 - Combinacion de isomerizacion de c5 a c6 y de adsorcion con oscilacion de la presion. - Google Patents
Combinacion de isomerizacion de c5 a c6 y de adsorcion con oscilacion de la presion.Info
- Publication number
- ES2055548T3 ES2055548T3 ES91311065T ES91311065T ES2055548T3 ES 2055548 T3 ES2055548 T3 ES 2055548T3 ES 91311065 T ES91311065 T ES 91311065T ES 91311065 T ES91311065 T ES 91311065T ES 2055548 T3 ES2055548 T3 ES 2055548T3
- Authority
- ES
- Spain
- Prior art keywords
- stream
- deisohexanizer
- hydrocarbons
- methylpentane
- recycle stream
- 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.)
- Expired - Lifetime
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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C9/00—Aliphatic saturated hydrocarbons
- C07C9/14—Aliphatic saturated hydrocarbons with five to fifteen carbon atoms
- C07C9/16—Branched-chain 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
- C10G67/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only
- C10G67/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only
- C10G67/06—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only plural serial stages only including a sorption process as the refining step in the absence of hydrogen
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)
- Crystallography & Structural Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
SE ISOMERIZAN HIDROCARBONOS C SUB 5 Y C SUB 6 EN UN PROCESO QUE COMBINA UN DEISOHEXANIZADOR CON UNA SECCION DE SEPARACION PSA PARA DAR UNA CORRIENTE DE PRODUCTO QUE COMPRENDE HIDROCARBONOS DE ALTA RAMIFICACION TALES COMO METILBUTANO Y DIMETILBUTANO. EL PROCESO COMBINA UNA METILPENTANO Y UNA CORRIENTE RECICLADA DE HEXANO NORMAL, UNA CORRIENTE RECICLADA PENTANO NORMAL Y AL MENOS UNA PORCION DE LOS HIDROCARBONOS C SUB 5 Y C SUB 6 DE LA CORRIENTE DE ALIMENTACION FRESCA PARA DAR UNA CORRIENTE DE ALIMENTACION COMBINADA QUE SE CARGA EN UNA ZONA DE ISOMERIZACION. EL EFLUENTE DE LA ZONA DE ISOMERIZACION SE ESTABILIZA Y PASA A UN DEISOHEXANIZADOR. UNA CORRIENTE DE CORTE LATERAL LLEVA EL METILPENTANO Y LA CORRIENTE DEL RECICLADO HEXANO DEL DISOHEXANIZADOR. LOS HIDROCARBONOS QUE TIENEN UN PUNTO DE EBULLICION MAS ALTO QUE LA CORRIENTE DE CORTE LATERAL SE EXTRAEN COMO CORRIENTES DE FONDO DEL DISOHEXANIZADOR. UNA SOBRE CABEZA TRANSPORTA EL PENTANO NORMAL, METILBUTANO Y DIMETILBUTANOS A LA SECCION DE SEPARACION PSA. SE RECUPERA UNA CORRIENTE EXTRACTO COMO LA CORRIENTE DE RECICLADO PENTANO NORMAL. EL REFINADO DEL PSA PROPORCIONA UNA CORRIENTE ISOMERATO DE ALTO OCTANAJE QUE CONSTA PRINCIPALMENTE DE METILPENTANO Y DIMETILBUTANOS.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/619,556 US5146037A (en) | 1990-11-29 | 1990-11-29 | Isomerization with distillation and psa recycle streams |
Publications (1)
Publication Number | Publication Date |
---|---|
ES2055548T3 true ES2055548T3 (es) | 1994-08-16 |
Family
ID=24482387
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES91311065T Expired - Lifetime ES2055548T3 (es) | 1990-11-29 | 1991-11-29 | Combinacion de isomerizacion de c5 a c6 y de adsorcion con oscilacion de la presion. |
Country Status (6)
Country | Link |
---|---|
US (1) | US5146037A (es) |
EP (1) | EP0488757B1 (es) |
AT (1) | ATE106374T1 (es) |
CA (1) | CA2056597C (es) |
DE (1) | DE69102249T2 (es) |
ES (1) | ES2055548T3 (es) |
Families Citing this family (40)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5246567A (en) * | 1992-02-10 | 1993-09-21 | Amoco Corporation | Benzene removal in an isomerization process |
US5365011A (en) * | 1992-05-29 | 1994-11-15 | The Boc Group, Inc. | Method of producing unsaturated hydrocarbons and separating the same from saturated hydrocarbons |
US5326926A (en) * | 1993-03-11 | 1994-07-05 | Uop | Isomerization with improved RVP and C4 recovery |
US5360534A (en) * | 1993-05-24 | 1994-11-01 | Uop | Isomerization of split-feed benzene-containing paraffinic feedstocks |
US5433770A (en) * | 1993-12-27 | 1995-07-18 | Uop | PSA process employing a rapid depressurization step to create a disequilibrium effect |
US5523503A (en) * | 1994-07-13 | 1996-06-04 | Uop | Cocurrent simulated moving bed hydrocarbon alkylation process |
US5792897A (en) * | 1994-09-23 | 1998-08-11 | Uop Llc | Hydrocardon recovery from corrosive effluent stream |
US5763730A (en) * | 1994-11-03 | 1998-06-09 | Uop | Process for alkane isomerization using reactive chromatography |
US5530173A (en) * | 1994-11-03 | 1996-06-25 | Funk; Gregory A. | Process for alkane isomerization using reactive chromatography and reactive desorbent |
US5530172A (en) * | 1994-11-03 | 1996-06-25 | Uop | Process for alkane isomerization using reactive chromatography |
US5744683A (en) * | 1996-06-18 | 1998-04-28 | Uop | Process for continuous reaction and deparation using reactive chromatography |
US5770783A (en) * | 1997-02-03 | 1998-06-23 | Uop Llc | Alkane isomerization using reversible flow reactive chromatography |
FR2771419B1 (fr) * | 1997-11-25 | 1999-12-31 | Inst Francais Du Petrole | Essences a haut indice d'octane et leur production par un procede associant hydro-isomerisation et separation |
FR2776667B1 (fr) * | 1998-03-31 | 2000-06-16 | Total Raffinage Distribution | Procede et dispositif d'isomerisation d'essences a teneur elevee en benzene |
US6069289A (en) * | 1998-08-31 | 2000-05-30 | Uop Llc | Process for separating and recovering multimethyl-branched alkanes |
FR2820754B1 (fr) * | 2001-02-12 | 2003-12-05 | Inst Francais Du Petrole | Dispositif comprenant un recyclage vers un separateur, et en melange avec une charge, de l'effluent liquide issu d'un absorbeur |
US6979396B2 (en) * | 2001-08-29 | 2005-12-27 | Uop Llc | Combination reforming and isomerization process |
US7435329B1 (en) | 2001-08-29 | 2008-10-14 | Uop Llc | Combination reforming and isomerization process |
US7015175B2 (en) * | 2001-08-29 | 2006-03-21 | Uop Llc | High-activity isomerization catalyst and process |
US7022889B2 (en) * | 2001-08-29 | 2006-04-04 | Uop Llc | Isomerization process using novel catalyst |
FR2862311B1 (fr) * | 2003-11-14 | 2008-05-30 | Inst Francais Du Petrole | Procede de production d'essences a haut indice d'octane a partir d'une coupe c5/c6 utilisant une unite de separation par menbrane |
US7223898B2 (en) * | 2005-03-11 | 2007-05-29 | Uop Llc | Isomerization process |
US7514590B1 (en) | 2005-03-11 | 2009-04-07 | Uop Llc | Isomerization process with adsorptive separation |
US7846322B2 (en) * | 2005-03-11 | 2010-12-07 | Uop Llc | Integrated refinery with enhanced olefin and reformate production |
US7638675B2 (en) * | 2007-09-07 | 2009-12-29 | Uop Llc | Processes for the isomerization of normal butane to isobutane |
US7638676B2 (en) * | 2007-09-07 | 2009-12-29 | Uop Llc | Processes for the isomerization of feedstocks comprising paraffins of 5 to 7 carbon atoms |
US7638674B2 (en) * | 2007-09-07 | 2009-12-29 | Uop Llc | Processes for the isomerization of paraffins of 5 and 6 carbon atoms with methylcyclopentane recovery |
US7812207B2 (en) * | 2007-09-07 | 2010-10-12 | Uop Llc | Membrane separation processes and systems for enhanced permeant recovery |
US8716544B2 (en) * | 2011-01-13 | 2014-05-06 | Uop Llc | Process for isomerizing a feed stream including one or more C4-C6 hydrocarbons |
US20130096356A1 (en) * | 2011-10-14 | 2013-04-18 | Uop Llc | Methods and apparatuses for the isomerization and deisohexanizing of hydrocarbon feeds |
US20140107382A1 (en) * | 2012-10-16 | 2014-04-17 | Uop Llc | Methods and apparatuses for separating a linear hexane stream from a hydrocarbon feed |
US20150051431A1 (en) * | 2013-08-15 | 2015-02-19 | Uop Llc | Methods and systems for producing gasoline |
US10654770B2 (en) | 2016-08-29 | 2020-05-19 | Exxonmobil Chemical Patents Inc. | Production of neopentane |
WO2018044592A1 (en) * | 2016-08-29 | 2018-03-08 | Exxonmobil Chemical Patents Inc. | Production of neopentane |
US10870610B2 (en) | 2016-08-29 | 2020-12-22 | Exxonmobil Chemical Patents Inc. | Production of neopentane |
US10487023B2 (en) | 2016-08-29 | 2019-11-26 | Exxonmobil Chemical Patents Inc. | Production of neopentane |
RU182214U1 (ru) * | 2017-12-21 | 2018-08-07 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Санкт-Петербургский государственный технологический институт (технический университет)" (СПбГТИ(ТУ)) | Установка для изомеризации легких бензиновых фракций |
US10994264B2 (en) | 2018-05-30 | 2021-05-04 | Exxonmobil Chemical Patents Inc. | Catalysts and processes for making catalysts for producing neopentane |
US10626064B2 (en) | 2018-05-30 | 2020-04-21 | Exxonmobil Chemical Patents Inc. | Processes to make neopentane using shell and tube reactors |
CN110898612A (zh) * | 2019-11-20 | 2020-03-24 | 复榆(张家港)新材料科技有限公司 | 一种c6烃吸附分离系统 |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2912473A (en) * | 1957-09-19 | 1959-11-10 | Pure Oil Co | Fractionation process using zeolitic molecular sieves |
US2921104A (en) * | 1957-11-08 | 1960-01-12 | Universal Oil Prod Co | Combination process of isomerization and selective fractionation followed by a sorption process |
US2966528A (en) * | 1957-11-08 | 1960-12-27 | Universal Oil Prod Co | Combination process of isomerization and a sorption process followed by selective frationation |
US3175444A (en) * | 1962-03-07 | 1965-03-30 | Morley Company | Measuring apparatus having a carriage advancing to feed workpiece and roller means feeding workpiece while carriage is retracting |
US3755144A (en) * | 1971-10-13 | 1973-08-28 | Universal Oil Prod Co | Hydrocarbon isomerization and separation process |
FR2184461B1 (es) * | 1972-05-17 | 1974-07-26 | Inst Francais Du Petrole | |
US4709117A (en) * | 1986-04-07 | 1987-11-24 | Union Carbide Corporation | Total isomerization process and apparatus |
US4709116A (en) * | 1986-06-30 | 1987-11-24 | Union Carbide Corporation | Isomerization process and apparatus |
US4717784A (en) * | 1986-12-10 | 1988-01-05 | Shell Oil Company | Total isomerization process with mono-methyl-branched plus normal paraffin recycle stream |
US4804803A (en) * | 1987-12-07 | 1989-02-14 | Uop Inc. | Isomerization with once-through hydrogen |
US4804802A (en) * | 1988-01-25 | 1989-02-14 | Shell Oil Company | Isomerization process with recycle of mono-methyl-branched paraffins and normal paraffins |
US4831209A (en) * | 1988-06-14 | 1989-05-16 | Amoco Corporation | Fractionation for a C6 paraffin isomerization process |
-
1990
- 1990-11-29 US US07/619,556 patent/US5146037A/en not_active Expired - Lifetime
-
1991
- 1991-11-28 CA CA002056597A patent/CA2056597C/en not_active Expired - Fee Related
- 1991-11-29 EP EP91311065A patent/EP0488757B1/en not_active Expired - Lifetime
- 1991-11-29 DE DE69102249T patent/DE69102249T2/de not_active Expired - Fee Related
- 1991-11-29 AT AT91311065T patent/ATE106374T1/de not_active IP Right Cessation
- 1991-11-29 ES ES91311065T patent/ES2055548T3/es not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
US5146037A (en) | 1992-09-08 |
EP0488757A1 (en) | 1992-06-03 |
CA2056597A1 (en) | 1992-05-30 |
ATE106374T1 (de) | 1994-06-15 |
EP0488757B1 (en) | 1994-06-01 |
DE69102249T2 (de) | 1994-09-15 |
CA2056597C (en) | 2002-04-02 |
DE69102249D1 (de) | 1994-07-07 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG2A | Definitive protection |
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