ES8700683A1 - Un metodo de anadir catalizador aditivo zsm-5 a la existencia de catalizador de una unidad de craqueo catalitico fluidizado. - Google Patents

Un metodo de anadir catalizador aditivo zsm-5 a la existencia de catalizador de una unidad de craqueo catalitico fluidizado.

Info

Publication number
ES8700683A1
ES8700683A1 ES544990A ES544990A ES8700683A1 ES 8700683 A1 ES8700683 A1 ES 8700683A1 ES 544990 A ES544990 A ES 544990A ES 544990 A ES544990 A ES 544990A ES 8700683 A1 ES8700683 A1 ES 8700683A1
Authority
ES
Spain
Prior art keywords
fluid bed
catalytic cracking
containing catalyst
bed catalytic
zsm
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
Application number
ES544990A
Other languages
English (en)
Other versions
ES544990A0 (es
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ExxonMobil Oil Corp
Original Assignee
Mobil Oil 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 Mobil Oil Corp filed Critical Mobil Oil Corp
Publication of ES544990A0 publication Critical patent/ES544990A0/es
Publication of ES8700683A1 publication Critical patent/ES8700683A1/es
Expired legal-status Critical Current

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
    • 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
    • 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
    • B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • 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
    • B01J29/80—Mixtures of different zeolites
    • 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
    • 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
    • C10G11/187—Controlling or regulating
    • 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
    • B01J2229/26—After treatment, characterised by the effect to be obtained to stabilize the total catalyst structure
    • 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
    • B01J2229/36—Steaming
    • 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
    • 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

Landscapes

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

Abstract

METODO DE INCORPORACION DE CATALIZADOR ZSM-5 EN UNA UNIDAD DE CRAQUEO CATALITICO FLUIDIZADO (FCC) QUE CONTIENE CATALIZADOR EN EQUILIBRIO. COMPRENDE LA ADICION DE CATALIZADOR ZSM-5 AL CATALIZADOR EN EQUILIBRIO, EN PROPORCION DE 1-20% DEL CATALIZADOR EN EQUILIBRIO QUE CIRCULA DENTRO DE LA UNIDAD FCC, DE MODO QUE INCREMENTA EL INDICE DE OCTANO DE RESEARCH DEL PRODUCTO DE GASOLINA DESDE 0,5 A 2,0 UNIDADES EN UN PERIODO DE 24 HORAS; SEGUIDAMENTE AÑADIR, SOBRE UNA BASE DIARIA, UNA CANTIDAD DECRECIENTE DE CATALIZADOR ZSM-5 PARA MANTENER EL AUMENTO DEL INDICE DE OCTANO AL NIVEL DESEADO. TIENE APLICACIONES PARA MEJORAR EL INDICE DE OCTANO DE LAS GASOLINAS.
ES544990A 1984-07-11 1985-07-09 Un metodo de anadir catalizador aditivo zsm-5 a la existencia de catalizador de una unidad de craqueo catalitico fluidizado. Expired ES8700683A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US62992284A 1984-07-11 1984-07-11

Publications (2)

Publication Number Publication Date
ES544990A0 ES544990A0 (es) 1986-10-16
ES8700683A1 true ES8700683A1 (es) 1986-10-16

Family

ID=24525033

Family Applications (1)

Application Number Title Priority Date Filing Date
ES544990A Expired ES8700683A1 (es) 1984-07-11 1985-07-09 Un metodo de anadir catalizador aditivo zsm-5 a la existencia de catalizador de una unidad de craqueo catalitico fluidizado.

Country Status (15)

Country Link
EP (1) EP0168979B1 (es)
JP (1) JPS6140397A (es)
AR (1) AR243584A1 (es)
AT (1) ATE45175T1 (es)
AU (1) AU571704B2 (es)
CA (1) CA1252411A (es)
DE (1) DE3572002D1 (es)
ES (1) ES8700683A1 (es)
FI (1) FI85717C (es)
GR (1) GR851686B (es)
IN (1) IN165201B (es)
MA (1) MA20482A1 (es)
PT (1) PT80795B (es)
TR (1) TR22322A (es)
ZA (1) ZA854825B (es)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4927523A (en) * 1988-12-12 1990-05-22 Mobil Oil Corporation Addition of shape selective zeolites to catalytic cracking units
GB9114390D0 (en) * 1991-07-03 1991-08-21 Shell Int Research Hydrocarbon conversion process and catalyst composition
WO1993022400A1 (en) * 1992-05-04 1993-11-11 Mobil Oil Corporation Fluidized catalytic cracking
US7582203B2 (en) 2004-08-10 2009-09-01 Shell Oil Company Hydrocarbon cracking process for converting gas oil preferentially to middle distillate and lower olefins
KR20070056090A (ko) 2004-08-10 2007-05-31 쉘 인터내셔날 리써취 마트샤피지 비.브이. 탄화수소 원료로 중간 증류 제품 및 저급 올레핀을 만드는방법 및 장치
US8920630B2 (en) 2007-04-13 2014-12-30 Shell Oil Company Systems and methods for making a middle distillate product and lower olefins from a hydrocarbon feedstock
RU2548362C2 (ru) * 2009-06-25 2015-04-20 Чайна Петролеум & Кемикал Корпорейшн Катализатор каталитического крекинга и способ повышения селективности катализатора(варианты)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3758403A (en) * 1970-10-06 1973-09-11 Mobil Oil Olites catalytic cracking of hydrocarbons with mixture of zsm-5 and other ze
US4309279A (en) * 1979-06-21 1982-01-05 Mobil Oil Corporation Octane and total yield improvement in catalytic cracking
ZA803517B (en) * 1979-06-21 1981-06-24 Mobil Oil Corp Octane improvement in catalytic cracking
US4309280A (en) * 1980-07-18 1982-01-05 Mobil Oil Corporation Promotion of cracking catalyst octane yield performance

Also Published As

Publication number Publication date
JPH0583594B2 (es) 1993-11-26
GR851686B (es) 1985-11-26
DE3572002D1 (en) 1989-09-07
AU571704B2 (en) 1988-04-21
IN165201B (es) 1989-08-26
FI85717C (fi) 1992-05-25
MA20482A1 (fr) 1986-04-01
EP0168979B1 (en) 1989-08-02
JPS6140397A (ja) 1986-02-26
AU4413785A (en) 1986-01-16
PT80795A (en) 1985-08-01
ATE45175T1 (de) 1989-08-15
FI852737L (fi) 1986-01-12
ZA854825B (en) 1987-02-25
ES544990A0 (es) 1986-10-16
CA1252411A (en) 1989-04-11
EP0168979A3 (en) 1986-12-10
AR243584A1 (es) 1993-08-31
FI852737A0 (fi) 1985-07-10
EP0168979A2 (en) 1986-01-22
PT80795B (pt) 1987-09-18
TR22322A (tr) 1987-02-10
FI85717B (fi) 1992-02-14

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Legal Events

Date Code Title Description
FD1A Patent lapsed

Effective date: 20040611