AR004874A1 - Catalizador para el craqueo catalítico fluido (fcc) de cargas de petróleo, proceso para elaborarlo y proceso para el craqueo catalítico de una carga de petróleo contaminada con al menos un metal seleccionado del grupo consistente en níquel y vanadio - Google Patents

Catalizador para el craqueo catalítico fluido (fcc) de cargas de petróleo, proceso para elaborarlo y proceso para el craqueo catalítico de una carga de petróleo contaminada con al menos un metal seleccionado del grupo consistente en níquel y vanadio

Info

Publication number
AR004874A1
AR004874A1 ARP960105521A ARP960105521A AR004874A1 AR 004874 A1 AR004874 A1 AR 004874A1 AR P960105521 A ARP960105521 A AR P960105521A AR P960105521 A ARP960105521 A AR P960105521A AR 004874 A1 AR004874 A1 AR 004874A1
Authority
AR
Argentina
Prior art keywords
catalyst
catalytic
oil
fcc
craquing
Prior art date
Application number
ARP960105521A
Other languages
English (en)
Original Assignee
Engelhard Corp
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 Engelhard Corp filed Critical Engelhard Corp
Publication of AR004874A1 publication Critical patent/AR004874A1/es

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
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10—After treatment, characterised by the effect to be obtained
    • B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
    • 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
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles

Landscapes

  • Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Closures For Containers (AREA)

Abstract

Se trata de catalizadores calcinados para el craque de cargas de petróleo que tienen zeolitas cristalinas en una matriz óxidos inorgánicos y que contienemenos de alrededor de 75% de Na2=, entre 0,1 y 10% de P expresado como P2P5, cuyosespectros tienen picos de alrededor de 3735 1/cm cuando son tratados conpiridina y se analizan mediante FTIR. Un proceso para elaborar un catalizador FCC caracterizado por poseer una alta tolerancia a los metales contaminados queconsiste enproporcionar mic roesferas catalizadoras de quebrado fluído que contienen zolite Y en una matriz de óxido inorgánico y analizar 20 a 60% porpeso Al2O3 y analizar de 0,75% en peso de Na2O; impregnar el catalizador una solución de fosfato o deuna sal de fosfat o en una cantidad de modo tal que lasmicroesferas analizan 0,5 a 10% por peso P2O5 y calcinar las microesferas en ausencia de vapor a una temperatura sobre 1300°F y por debajo de 1600°F yrecuperar el producto que se caracterizapor un pico de 3867 1/cm es superior a aproximadamente 0,8
ARP960105521A 1995-12-08 1996-12-06 Catalizador para el craqueo catalítico fluido (fcc) de cargas de petróleo, proceso para elaborarlo y proceso para el craqueo catalítico de una carga de petróleo contaminada con al menos un metal seleccionado del grupo consistente en níquel y vanadio AR004874A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US56981095A 1995-12-08 1995-12-08

Publications (1)

Publication Number Publication Date
AR004874A1 true AR004874A1 (es) 1999-03-10

Family

ID=24276958

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP960105521A AR004874A1 (es) 1995-12-08 1996-12-06 Catalizador para el craqueo catalítico fluido (fcc) de cargas de petróleo, proceso para elaborarlo y proceso para el craqueo catalítico de una carga de petróleo contaminada con al menos un metal seleccionado del grupo consistente en níquel y vanadio

Country Status (3)

Country Link
US (1) US5993645A (es)
AR (1) AR004874A1 (es)
CO (1) CO4790165A1 (es)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030089640A1 (en) * 2001-10-17 2003-05-15 Rostam Madon FCC catalysts for feeds containing nickel and vanadium
US6656347B2 (en) 2000-09-22 2003-12-02 Engelhard Corporation Structurally enhanced cracking catalysts
US6673235B2 (en) 2000-09-22 2004-01-06 Engelhard Corporation FCC catalysts for feeds containing nickel and vanadium
US6696378B2 (en) 2001-08-31 2004-02-24 Engelhard Corporation Fluid catalytic cracking catalyst manufacturing process
JP4463556B2 (ja) * 2001-10-17 2010-05-19 バスフ・カタリスツ・エルエルシー ニッケルとバナジウムを含有する供給材料用のｆｃｃ触媒
US7101473B2 (en) 2002-05-31 2006-09-05 Engelhard Corporation Method of enhancing the activity of FCC catalysts
US6942783B2 (en) * 2003-05-19 2005-09-13 Engelhard Corporation Enhanced FCC catalysts for gas oil and resid applications
WO2011154973A1 (en) 2010-06-07 2011-12-15 Indian Oil Corporation Limited Metal passivator additive and process for preparing
IN2014CN04033A (es) * 2011-11-04 2015-10-23 Basf Corp
US9796932B2 (en) * 2013-12-19 2017-10-24 Basf Corporation FCC catalyst compositions containing boron oxide and phosphorus
US20150174559A1 (en) * 2013-12-19 2015-06-25 Basf Corporation Phosphorus-Modified FCC Catalysts

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3506594A (en) * 1968-06-20 1970-04-14 Engelhard Min & Chem Microspherical zeolitic molecular sieve composite catalyst and preparation thereof
US3663165A (en) * 1970-02-09 1972-05-16 Engelhard Min & Chem Zeolitic catalyst and preparation
US4430199A (en) * 1981-05-20 1984-02-07 Engelhard Corporation Passivation of contaminant metals on cracking catalysts by phosphorus addition
US4454241A (en) * 1982-05-24 1984-06-12 Exxon Research And Engineering Co. Phosphorus-containing catalyst
US4493902A (en) * 1983-02-25 1985-01-15 Engelhard Corporation Fluid catalytic cracking catalyst comprising microspheres containing more than about 40 percent by weight Y-faujasite and methods for making
CA1297861C (en) * 1986-07-11 1992-03-24 William L. Schuette Hydrocarbon cracking catalysts and processes utilizing the same
US5023220A (en) * 1988-11-16 1991-06-11 Engelhard Corporation Ultra high zeolite content FCC catalysts and method for making same from microspheres composed of a mixture of calcined kaolin clays
US4977122A (en) * 1989-06-05 1990-12-11 Exxon Research And Engineering Company Cracking catalyst
US5243121A (en) * 1992-03-19 1993-09-07 Engelhard Corporation Fluid catalytic cracking process for increased formation of isobutylene and isoamylenes
US5427753A (en) * 1992-12-24 1995-06-27 Tosoh Corporation Process for removing nitrogen oxides from oxygen rich exhaust gas
US5395809A (en) * 1993-11-01 1995-03-07 Engelhard Corporation Modified microsphere FCC catalysts
US5559067A (en) * 1995-03-31 1996-09-24 Engelhard Corporation Modified microsphere FCC catalysts and manufacture thereof

Also Published As

Publication number Publication date
CO4790165A1 (es) 1999-05-31
US5993645A (en) 1999-11-30

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