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AR015038A1 - Un proceso de craqueo catalitico de fluidos conducido bajo condiciones de craqueo catalitico - Google Patents

Un proceso de craqueo catalitico de fluidos conducido bajo condiciones de craqueo catalitico

Info

Publication number
AR015038A1
AR015038A1 ARP990101978A ARP990101978A AR015038A1 AR 015038 A1 AR015038 A1 AR 015038A1 AR P990101978 A ARP990101978 A AR P990101978A AR P990101978 A ARP990101978 A AR P990101978A AR 015038 A1 AR015038 A1 AR 015038A1
Authority
AR
Argentina
Prior art keywords
fcc
differ
feeds
fluid
approximately
Prior art date
Application number
ARP990101978A
Other languages
English (en)
Original Assignee
Exxon Research Engineering Co
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 Exxon Research Engineering Co filed Critical Exxon Research Engineering Co
Publication of AR015038A1 publication Critical patent/AR015038A1/es

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S208/00Mineral oils: processes and products
    • Y10S208/01Automatic control

Landscapes

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

Abstract

Un proceso de craqueo catalítico de fluido conducido bajo condiciones de craqueo catalítico de fluido que permite un mayor uso de alimentacionesalternativas y mejores rendimientos de productos deseados. El producto descripto se relaciona con el craqueo catalítico de fluidos (FCC) para la produccion decombustibles líquidos y olefinas livianas a partir de mezclas de hidrocarburos tales como fracciones de petroleo. Más en particular, se relaciona con unacaracterística no lineal del proceso de FCC que conduce a una nueva estrategia de operacion de FCC para la conversion de mezclas de hidrocarburos. El método deoperacion de FCC se ha perfeccionado para el craqueo de alimentaciones de diferentes cualidades, teniendo en cuenta que el rendimiento líquido en el FCC no sedegrada en forma lineal, ni el rendimiento de coque incrementa en forma lineal, a medida que la cantidad de componente pesado en la alimentacion incrementa, yen consecuencia que el efecto marginal nocivo de los contaminantes dela alimentacion en el catalizador de FCC se torna incrementadamente más débil concantidades en aumento de componentes pesados. El proceso de FCC conducido bajo condiciones de craqueo catalítico descripto, comprende inyectar en por lo menosuna zona dereaccion de una unidad de craqueo catalítica de fluido (FCCU), que tiene uno o más tubos verticales, una pluralidad de alimentaciones, en dondedicha pluralidad de alimentaciones comprende por lo menos una alimentacion (alfa) y por lo menos otra alimentacion (beta), en donde dichas alimentaciones(alfa) y (beta): (a) difieren en Residuo de Carbono Conradson por lo menos aproximadamente en un 2% en peso puntos, o (b) difieren en contenido de hidrogenopor lo menos aproximadamente en un 0,2% en peso; o (c) difieren en gravedades API por lo menos aproximadamente por 2 puntos; o (d) difieren en contenido denitrogeno por lo menos aproximadamente por 50ppm; o (e) difieren en la relacion de carbono a hidrogeno por lo menos aproximadamente por 0,3; o(f) difieren enpunto de ebullicion medio por lo menos aproximadamente 93,33 *C (200 *F); y en donde dichas alimentaciones (alfa) y (beta) son alternadamente inyectadas y en
ARP990101978A 1998-04-28 1999-04-28 Un proceso de craqueo catalitico de fluidos conducido bajo condiciones de craqueo catalitico AR015038A1 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US6787098A 1998-04-28 1998-04-28
US09/294,951 US6156189A (en) 1998-04-28 1999-04-20 Operating method for fluid catalytic cracking involving alternating feed injection

Publications (1)

Publication Number Publication Date
AR015038A1 true AR015038A1 (es) 2001-04-11

Family

ID=22078969

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP990101978A AR015038A1 (es) 1998-04-28 1999-04-28 Un proceso de craqueo catalitico de fluidos conducido bajo condiciones de craqueo catalitico

Country Status (2)

Country Link
US (1) US6156189A (es)
AR (1) AR015038A1 (es)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR0205585A (pt) * 2002-10-29 2004-08-03 Petroleo Brasileiro Sa Processo para craqueamento catalìtico fluido de cargas de hidrocarbonetos com altos teores de nitrogênio básico
JP2007258481A (ja) * 2006-03-23 2007-10-04 Fujitsu Ltd 半導体装置及びその製造方法
US8246914B2 (en) * 2008-12-22 2012-08-21 Uop Llc Fluid catalytic cracking system
US9394488B2 (en) 2012-04-19 2016-07-19 Exxonmobil Research And Engineering Company Method for optimizing catalyst/oil mixing in an FCC reactor feed zone

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3424672A (en) * 1967-01-09 1969-01-28 Phillips Petroleum Co Fluid catalytic stripping
US3448037A (en) * 1968-06-18 1969-06-03 Dorrance P Bunn Jr Cracking with crystalline zeolite catalyst
US3617496A (en) * 1969-06-25 1971-11-02 Gulf Research Development Co Fluid catalytic cracking process with a segregated feed charged to separate reactors
JPS4911603B1 (es) * 1970-12-02 1974-03-18
US3781533A (en) * 1972-04-07 1973-12-25 Exxon Research Engineering Co Constraint control system for optimizing performance of process units
US3801493A (en) * 1972-10-25 1974-04-02 Texaco Inc Slack wax cracking in an fccu with a satellite reactor
US3993556A (en) * 1972-12-11 1976-11-23 Texaco Inc. Method of catalytic cracking of hydrocarbons
US3928172A (en) * 1973-07-02 1975-12-23 Mobil Oil Corp Catalytic cracking of FCC gasoline and virgin naphtha
NL8403551A (nl) * 1984-11-22 1986-06-16 Shell Int Research Werkwijze voor de bereiding van benzine.
US4826586A (en) * 1986-09-03 1989-05-02 Mobil Coil Corporation Single riser fluidized catalytic cracking process utilizing a C3-4 paraffin-rich co-feed and mixed catalyst system
CA1327177C (en) * 1988-11-18 1994-02-22 Alan R. Goelzer Process for selectively maximizing product production in fluidized catalytic cracking of hydrocarbons
US4927522A (en) * 1988-12-30 1990-05-22 Mobil Oil Corporation Multiple feed point catalytic cracking process using elutriable catalyst mixture
DE69007649T2 (de) * 1989-02-06 1994-08-25 Stone & Webster Eng Corp Verfahren zur katalytischen Krackung von Kohlenwasserstoffen.
US5009769A (en) * 1989-02-06 1991-04-23 Stone & Webster Engineering Corporation Process for catalytic cracking of hydrocarbons
US5108580A (en) * 1989-03-08 1992-04-28 Texaco Inc. Two catalyst stage hydrocarbon cracking process
US5298155A (en) * 1990-02-27 1994-03-29 Exxon Research & Engineering Co. Controlling yields and selectivity in a fluid catalytic cracker unit
US5098554A (en) * 1990-03-02 1992-03-24 Chevron Research Company Expedient method for altering the yield distribution from fluid catalytic cracking units
US5188805A (en) * 1990-07-03 1993-02-23 Exxon Research And Engineering Company Controlling temperature in a fluid hydrocarbon conversion and cracking apparatus and process comprising a novel feed injection system
US5435906A (en) * 1992-08-20 1995-07-25 Stone & Webster Engineering Corporation Process for catalytically cracking feedstocks paraffin rich comprising high and low concarbon components
CN1089641A (zh) * 1992-08-20 1994-07-20 史东及韦伯斯特工程公司 含高和低康拉逊残炭组分的富石蜡原料的催化裂化方法

Also Published As

Publication number Publication date
US6156189A (en) 2000-12-05

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