MX352408B - Proceso para reducir el contenido de benceno de la gasolina. - Google Patents

Proceso para reducir el contenido de benceno de la gasolina.

Info

Publication number
MX352408B
MX352408B MX2014001749A MX2014001749A MX352408B MX 352408 B MX352408 B MX 352408B MX 2014001749 A MX2014001749 A MX 2014001749A MX 2014001749 A MX2014001749 A MX 2014001749A MX 352408 B MX352408 B MX 352408B
Authority
MX
Mexico
Prior art keywords
alkylation reaction
alkylating agent
reducing
reaction zone
alkylation
Prior art date
Application number
MX2014001749A
Other languages
English (en)
Other versions
MX2014001749A (es
Inventor
H Hwang Shyh-Yuan
Birkhoff Ronald
F Guarino Richard
Erik Moy J
Pherwani Geeta
Original Assignee
Badger Licensing Llc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Badger Licensing Llc filed Critical Badger Licensing Llc
Publication of MX2014001749A publication Critical patent/MX2014001749A/es
Publication of MX352408B publication Critical patent/MX352408B/es

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
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/54—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
    • C07C2/64—Addition to a carbon atom of a six-membered aromatic ring
    • C07C2/66—Catalytic processes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65
    • 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
    • C10G2300/104—Light gasoline having a boiling range of about 20 - 100 °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
    • C10G2300/10—Feedstock materials
    • C10G2300/1088—Olefins
    • 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
    • C10G2300/1096—Aromatics or polyaromatics

Abstract

La presente invención se refiere a un proceso para alquilar el benceno contenido en una corriente de gasolina de la refinería, en el cual se pone en contacto la corriente de gasolina de la refinería con un agente de alquilación que comprende una o más de las olefinas de C2 a C5 en una zona de reacción de alquilación bajo las condiciones de la alquilación para producir un efluente alquilado. La zona de reacción de la alquilación comprende al menos una primera etapa de la reacción de alquilación y una segunda etapa de la reacción de alquilación, y una porción del agente de alquilación es alimentado a cada una de la primera y segunda etapas de la reacción de alquilación de modo que, aunque la proporción molar de las substancias aromáticas que se pueden alquilar con respecto al agente de alquilación en la alimentación total para la zona de la reacción de alquilación es menor que 1, la proporción molar de las substancias aromáticas que se pueden alquilar con respecto al agente de alquilación en la entrada de cada una de las primera y segunda etapas de la reacción de alquilación es de al menos 1.0.
MX2014001749A 2011-08-19 2011-11-30 Proceso para reducir el contenido de benceno de la gasolina. MX352408B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
USPCT/US2011/048463 2011-08-19
PCT/US2011/062635 WO2013028215A1 (en) 2011-08-19 2011-11-30 Process for reducing the benzene content gasoline

Publications (2)

Publication Number Publication Date
MX2014001749A MX2014001749A (es) 2014-07-30
MX352408B true MX352408B (es) 2017-11-23

Family

ID=45401161

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2014001749A MX352408B (es) 2011-08-19 2011-11-30 Proceso para reducir el contenido de benceno de la gasolina.

Country Status (8)

Country Link
EP (1) EP2744875B1 (es)
JP (1) JP2014524509A (es)
KR (1) KR20140048971A (es)
CN (1) CN103797091B (es)
AU (1) AU2011375417B8 (es)
MX (1) MX352408B (es)
TW (1) TW201309788A (es)
WO (1) WO2013028215A1 (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9200215B2 (en) 2011-02-07 2015-12-01 Badger Licensing Llc Process for reducing the benzene content of gasoline
EP2673245B1 (en) 2011-02-07 2020-08-05 Badger Licensing LLC Process for reducing the benzene content of gasoline by alkylating benzene using a lower olefin in the presence of a paraffinic diluent
US9199891B2 (en) 2011-02-07 2015-12-01 Badger Licensing Llc Process for reducing the benzene content of gasoline

Family Cites Families (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3755483A (en) 1972-04-28 1973-08-28 Mobil Oil Vapor phase alkylation in presence of crystalline aluminosilicate catalyst
US3751504A (en) 1972-05-12 1973-08-07 Mobil Oil Corp Vapor-phase alkylation in presence of crystalline aluminosilicate catalyst with separate transalkylation
US4016218A (en) 1975-05-29 1977-04-05 Mobil Oil Corporation Alkylation in presence of thermally modified crystalline aluminosilicate catalyst
US4393262A (en) 1978-12-14 1983-07-12 Mobil Oil Corporation Production of isopropylbenzene
IT1127296B (it) * 1979-12-19 1986-05-21 Euteco Impianti Spa Procedimento perfezionato per la produzione di cumene
US4547605A (en) 1983-09-28 1985-10-15 Mobil Oil Corporation Catalyst for alkylation of aromatic hydrocarbons
US4582815A (en) 1984-07-06 1986-04-15 Mobil Oil Corporation Extrusion of silica-rich solids
US5149894A (en) 1986-01-29 1992-09-22 Chevron Research And Technology Company Alkylation using zeolite SSZ-25
US4954663A (en) 1988-10-06 1990-09-04 Mobil Oil Corp. Process for preparing long chain alkyl phenols
US4962256A (en) 1988-10-06 1990-10-09 Mobil Oil Corp. Process for preparing long chain alkyl aromatic compounds
US4954325A (en) 1986-07-29 1990-09-04 Mobil Oil Corp. Composition of synthetic porous crystalline material, its synthesis and use
US4908120A (en) 1987-08-20 1990-03-13 Mobil Oil Corporation Catalytic dewaxing process using binder-free zeolite
US4891458A (en) 1987-12-17 1990-01-02 Innes Robert A Liquid phase alkylation or transalkylation process using zeolite beta
US5001295A (en) 1988-10-06 1991-03-19 Mobil Oil Corp. Process for preparing dialkylnaphthalene
US4992606A (en) 1988-10-06 1991-02-12 Mobil Oil Corp. Process for preparing short chain alkyl aromatic compounds
US5043501A (en) 1990-03-15 1991-08-27 Mobil Oil Corp. Process for preparing dimethylnaphthalene
US5250777A (en) 1990-04-02 1993-10-05 Inductotherm Corp. Method and apparatus for variable phase induction heating and stirring
US5334795A (en) 1990-06-28 1994-08-02 Mobil Oil Corp. Production of ethylbenzene
EP0485683B1 (en) * 1990-11-13 2001-01-10 Fina Technology, Inc. Preparation of alkylated aromatics
US5120890A (en) * 1990-12-31 1992-06-09 Uop Process for reducing benzene content in gasoline
US5229341A (en) 1991-01-11 1993-07-20 Mobil Oil Corp. Crystalline oxide material
US5236575A (en) 1991-06-19 1993-08-17 Mobil Oil Corp. Synthetic porous crystalline mcm-49, its synthesis and use
US5545788A (en) 1991-06-19 1996-08-13 Mobil Oil Corporation Process for the alkylation of benzene-rich reformate using MCM-49
US5284643A (en) 1992-12-10 1994-02-08 Mobil Oil Corp. Gallium-containing zeolite MCM-22
US5362697A (en) 1993-04-26 1994-11-08 Mobil Oil Corp. Synthetic layered MCM-56, its synthesis and use
US6008422A (en) * 1997-07-14 1999-12-28 Uop Llc Alkylation process using interbed recycling of cooled reactor effluent
US7476774B2 (en) * 2005-02-28 2009-01-13 Exxonmobil Research And Engineering Company Liquid phase aromatics alkylation process
US20060194998A1 (en) * 2005-02-28 2006-08-31 Umansky Benjamin S Process for making high octane gasoline with reduced benzene content
US8395006B2 (en) * 2009-03-13 2013-03-12 Exxonmobil Research And Engineering Company Process for making high octane gasoline with reduced benzene content by benzene alkylation at high benzene conversion

Also Published As

Publication number Publication date
WO2013028215A1 (en) 2013-02-28
AU2011375417B8 (en) 2017-08-17
KR20140048971A (ko) 2014-04-24
MX2014001749A (es) 2014-07-30
JP2014524509A (ja) 2014-09-22
AU2011375417B2 (en) 2017-04-27
AU2011375417A8 (en) 2017-08-17
AU2011375417A1 (en) 2014-02-20
EP2744875B1 (en) 2016-08-03
CN103797091A (zh) 2014-05-14
CN103797091B (zh) 2016-07-06
TW201309788A (zh) 2013-03-01
EP2744875A1 (en) 2014-06-25

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