AR047402A1 - REDUCTION OF SULFUR IN GASOLINE USING HYDROTALCITE TYPE COMPOUNDS - Google Patents

REDUCTION OF SULFUR IN GASOLINE USING HYDROTALCITE TYPE COMPOUNDS

Info

Publication number
AR047402A1
AR047402A1 ARP040104460A ARP040104460A AR047402A1 AR 047402 A1 AR047402 A1 AR 047402A1 AR P040104460 A ARP040104460 A AR P040104460A AR P040104460 A ARP040104460 A AR P040104460A AR 047402 A1 AR047402 A1 AR 047402A1
Authority
AR
Argentina
Prior art keywords
gasoline
sulfur
type compounds
hydrotalcite
reduction
Prior art date
Application number
ARP040104460A
Other languages
Spanish (es)
Original Assignee
Intercat Inc
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
Priority claimed from US10/729,270 external-priority patent/US7431825B2/en
Application filed by Intercat Inc filed Critical Intercat Inc
Publication of AR047402A1 publication Critical patent/AR047402A1/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084—Y-type faujasite
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/16—Clays or other mineral silicates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/005—Spinels
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/007—Mixed salts
    • B01J35/19—
    • 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
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • C10G11/182—Regeneration
    • 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
    • C10G25/00—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
    • C10G25/003—Specific sorbent material, not covered by C10G25/02 or C10G25/03
    • 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
    • C10G25/00—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents
    • C10G25/06—Refining of hydrocarbon oils in the absence of hydrogen, with solid sorbents with moving sorbents or sorbents dispersed in the 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
    • C10G55/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
    • C10G55/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only
    • C10G55/06—Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only including at least one catalytic cracking step
    • 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
    • C10G2400/02—Gasoline

Abstract

La presente describe métodos novedosos para reducir el azufre en la gasolina con aditivos de compuestos tipo hidrotalcita, compuestos tipo hidrotalcita calcinados y/o soluciones solidas de oxidos metálicos mixtos. Los aditivos pueden contener adicionalmente de forma opcional uno o más oxidantes metálicos o soportes. La presente también se dirige a métodos para reducir el azufre en la gasolina que comprenden poner en contacto una reserva de alimentacion para craqueo catalítico con un compuesto de oxidos metálicos mixtos que contiene magnesio y aluminio y posee un patron de difraccion de rayos X que presenta al menos una reflexion en una posicion de pico dos Theta alrededor de 43 grados y alrededor de 62, en donde la razon entre magnesio y aluminio en el compuesto está entre alrededor de 1:1 y alrededor de 10:1.This discloses novel methods for reducing sulfur in gasoline with additives of hydrotalcite-like compounds, calcined hydrotalcite-type compounds and / or solid solutions of mixed metal oxides. The additives may additionally contain one or more metal oxidizers or supports. This is also directed to methods to reduce sulfur in gasoline that comprise contacting a feed pool for catalytic cracking with a compound of mixed metal oxides containing magnesium and aluminum and possessing an X-ray diffraction pattern that presents the minus a reflection in a two-theta peak position around 43 degrees and around 62, where the ratio between magnesium and aluminum in the compound is between about 1: 1 and about 10: 1.

ARP040104460A 2003-12-05 2004-11-30 REDUCTION OF SULFUR IN GASOLINE USING HYDROTALCITE TYPE COMPOUNDS AR047402A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/729,270 US7431825B2 (en) 2003-12-05 2003-12-05 Gasoline sulfur reduction using hydrotalcite like compounds
US10/749,695 US7347929B2 (en) 2003-12-05 2003-12-31 Gasoline sulfur reduction using hydrotalcite like compounds

Publications (1)

Publication Number Publication Date
AR047402A1 true AR047402A1 (en) 2006-01-18

Family

ID=34915761

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP040104460A AR047402A1 (en) 2003-12-05 2004-11-30 REDUCTION OF SULFUR IN GASOLINE USING HYDROTALCITE TYPE COMPOUNDS

Country Status (7)

Country Link
EP (1) EP1702027A4 (en)
JP (1) JP2007517925A (en)
KR (1) KR20060124664A (en)
AR (1) AR047402A1 (en)
AU (1) AU2004316294B2 (en)
CA (1) CA2548167C (en)
WO (1) WO2005081715A2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5269321B2 (en) * 2007-01-11 2013-08-21 株式会社Ａｄｅｋａ Desulfurization agent for ultra-deep oxidative desulfurization and oxidative desulfurization method using the same
US9211525B2 (en) * 2008-07-30 2015-12-15 Saudi Arabian Oil Company Metallic clay based FCC gasoline sulfur reduction additive compositions
TW202202226A (en) * 2020-07-14 2022-01-16 美商Ｗ．Ｒ．康格雷氏公司 Process for catalytic cracking and equilibrium fcc catalyst

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5399329A (en) * 1993-07-06 1995-03-21 Aristech Chemical Corporation Hydrotalcite-like materials having a sheet-like morphology and process for production thereof
US6028023A (en) * 1997-10-20 2000-02-22 Bulldog Technologies U.S.A., Inc. Process for making, and use of, anionic clay materials
US5951851A (en) * 1997-10-31 1999-09-14 Poirier; Marc-Andre Sulfur removal from hydrocarbon fluids by contacting said fluids with hydrololcite-like adsorbent material
NO317500B1 (en) * 1998-03-13 2004-11-08 Statoil Asa Process and composition for reducing the sulfur content of a hydrocarbon mixture, and use thereof
JP2003507303A (en) * 1999-08-11 2003-02-25 アクゾ ノーベル ナムローゼ フェンノートシャップ Abrasion-resistant, shaped bodies containing crystalline anionic clay
EP1517747A1 (en) * 2002-06-28 2005-03-30 Albemarle Netherlands B.V. Fcc catalyst for reducing the sulfur content in gasoline and diesel

Also Published As

Publication number Publication date
CA2548167A1 (en) 2005-09-09
WO2005081715A2 (en) 2005-09-09
AU2004316294B2 (en) 2010-05-27
EP1702027A2 (en) 2006-09-20
AU2004316294A1 (en) 2005-09-09
CA2548167C (en) 2009-09-22
KR20060124664A (en) 2006-12-05
WO2005081715A3 (en) 2006-05-18
JP2007517925A (en) 2007-07-05
EP1702027A4 (en) 2011-01-12

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