MX345633B - Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc. - Google Patents

Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc.

Info

Publication number
MX345633B
MX345633B MX2009000384A MX2009000384A MX345633B MX 345633 B MX345633 B MX 345633B MX 2009000384 A MX2009000384 A MX 2009000384A MX 2009000384 A MX2009000384 A MX 2009000384A MX 345633 B MX345633 B MX 345633B
Authority
MX
Mexico
Prior art keywords
fcc unit
catalyst
paraffinic
downflow reactor
cracking
Prior art date
Application number
MX2009000384A
Other languages
English (en)
Other versions
MX2009000384A (es
Inventor
f dean Christopher
Original Assignee
Saudi Arabian Oil Company *
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 Saudi Arabian Oil Company * filed Critical Saudi Arabian Oil Company *
Publication of MX2009000384A publication Critical patent/MX2009000384A/es
Publication of MX345633B publication Critical patent/MX345633B/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
    • 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
    • C10G51/00Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only
    • C10G51/06Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more cracking processes only plural parallel stages only
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J38/00Regeneration or reactivation of catalysts, in general
    • 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
    • C10G11/182Regeneration
    • 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
    • C10G55/00Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process
    • C10G55/02Treatment of hydrocarbon oils, in the absence of hydrogen, by at least one refining process and at least one cracking process plural serial stages only
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1037Hydrocarbon fractions
    • C10G2300/1044Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C
    • 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
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40Characteristics of the process deviating from typical ways of processing
    • C10G2300/4093Catalyst stripping
    • 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02Gasoline
    • 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
    • C10G2400/00Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20C2-C4 olefins

Landscapes

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

Abstract

La producción de hidrocarburos ligeros que consisten de etileno, propileno, butilenos y de gasolina es aumentada mediante la introducción de una corriente de alimentación de nafta parafínica virgen derivada de una fuente externa hacia un reactor secundario de flujo descendente que utiliza la misma composición de catalizador que una unidad de FCC adyacente para fraccionar la nafta y extraer la corriente del producto de reacción de hidrocarburo más ligero deseado del reactor de flujo descendente y regenerar el catalizador en el mismo recipiente de regeneración que se usa para regenerar el catalizador gastado de la unidad de FCC. La eficiencia de la recuperación de los hidrocarburos olefínicos más ligeros deseados se maximiza limitando la corriente de alimentación al reactor de flujo descendente a nafta parafínica que puede ser procesada bajo condiciones relativamente más severas, mientras que se minimiza la producción de subproductos indeseados y se reduce la formación de coque en el catalizador.
MX2009000384A 2006-07-13 2007-07-13 Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc. MX345633B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US11/487,022 US20080011645A1 (en) 2006-07-13 2006-07-13 Ancillary cracking of paraffinic naphtha in conjuction with FCC unit operations
PCT/US2007/016054 WO2008008527A2 (en) 2006-07-13 2007-07-13 Ancillary cracking of paraffinic naptha in conjunction with fcc unit operations

Publications (2)

Publication Number Publication Date
MX2009000384A MX2009000384A (es) 2009-04-06
MX345633B true MX345633B (es) 2017-02-08

Family

ID=38923953

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2009000384A MX345633B (es) 2006-07-13 2007-07-13 Craqueo secundario de nafta parafínica en conjunto con operaciones de la unidad de fcc.

Country Status (11)

Country Link
US (2) US20080011645A1 (es)
EP (1) EP2052058A4 (es)
JP (1) JP5424879B2 (es)
KR (1) KR101526608B1 (es)
CN (1) CN101501164B (es)
BR (1) BRPI0713183B1 (es)
CA (1) CA2657628C (es)
EA (1) EA017596B1 (es)
MX (1) MX345633B (es)
NO (1) NO20090152L (es)
WO (1) WO2008008527A2 (es)

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US11420915B2 (en) 2020-06-11 2022-08-23 Saudi Arabian Oil Company Red mud as a catalyst for the isomerization of olefins
US11495814B2 (en) 2020-06-17 2022-11-08 Saudi Arabian Oil Company Utilizing black powder for electrolytes for flow batteries
US11583824B2 (en) 2020-06-18 2023-02-21 Saudi Arabian Oil Company Hydrogen production with membrane reformer
US12000056B2 (en) 2020-06-18 2024-06-04 Saudi Arabian Oil Company Tandem electrolysis cell
US11999619B2 (en) 2020-06-18 2024-06-04 Saudi Arabian Oil Company Hydrogen production with membrane reactor
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US11505754B2 (en) 2020-09-01 2022-11-22 Saudi Arabian Oil Company Processes for producing petrochemical products from atmospheric residues
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US11814289B2 (en) 2021-01-04 2023-11-14 Saudi Arabian Oil Company Black powder catalyst for hydrogen production via steam reforming
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Also Published As

Publication number Publication date
EA017596B1 (ru) 2013-01-30
CA2657628C (en) 2015-11-10
EP2052058A2 (en) 2009-04-29
EP2052058A4 (en) 2011-11-16
WO2008008527A2 (en) 2008-01-17
US20080011645A1 (en) 2008-01-17
JP5424879B2 (ja) 2014-02-26
MX2009000384A (es) 2009-04-06
NO20090152L (no) 2009-04-02
KR101526608B1 (ko) 2015-06-05
BRPI0713183B1 (pt) 2017-03-07
BRPI0713183A2 (pt) 2012-04-17
CN101501164A (zh) 2009-08-05
KR20090043514A (ko) 2009-05-06
EA200900185A1 (ru) 2009-06-30
CN101501164B (zh) 2013-08-28
US20110240520A1 (en) 2011-10-06
JP2009543899A (ja) 2009-12-10
WO2008008527A3 (en) 2008-04-24
CA2657628A1 (en) 2008-01-17

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