AR008190A1 - Proceso para el hidrocraqueo de fracciones petroliferas pesadas - Google Patents

Proceso para el hidrocraqueo de fracciones petroliferas pesadas

Info

Publication number
AR008190A1
AR008190A1 ARP970104211A ARP970104211A AR008190A1 AR 008190 A1 AR008190 A1 AR 008190A1 AR P970104211 A ARP970104211 A AR P970104211A AR P970104211 A ARP970104211 A AR P970104211A AR 008190 A1 AR008190 A1 AR 008190A1
Authority
AR
Argentina
Prior art keywords
products
stream
heavy oil
boiling
mpa
Prior art date
Application number
ARP970104211A
Other languages
English (en)
Original Assignee
Bruge David
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 Bruge David filed Critical Bruge David
Publication of AR008190A1 publication Critical patent/AR008190A1/es

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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions

Landscapes

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

Abstract

La hidroconversión de fracciones petrolíferas pesadas que hierven principalmente por encima de 204*C (400*F) se realiza en un reactor de columnade destilación, donde en forma concurrente se alimenta un caudal de petróleo se destila ycontac ta en presencia de un catalizador de craqueo preparado en formade una estructura de destilacicón catalítica a una presión total de menos de aproximadamente 2068 MPa (300psig) y a una presión parcial de hidrógeno en laescala de 0,006 a0,482 MPa (1 0o a menos de 70 psia) y a una temperatura en la escala de 204* - 538*C (400 a 1000 F), donde una porción del caudal de petróleose craquea para obtener productos más livianos que bullen por debajo del punto de ebullición de laalimentación y los p roductos son destilados para extraerun caudal vaporoso de materiales superiores que comprende productos que bullen principalmente por debajo del punto de ebullición de la alimentación y uncaudal líquido de materialesresiduales.
ARP970104211A 1996-09-23 1997-09-12 Proceso para el hidrocraqueo de fracciones petroliferas pesadas AR008190A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US08/717,935 US5961815A (en) 1995-08-28 1996-09-23 Hydroconversion process

Publications (1)

Publication Number Publication Date
AR008190A1 true AR008190A1 (es) 1999-12-09

Family

ID=24884115

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP970104211A AR008190A1 (es) 1996-09-23 1997-09-12 Proceso para el hidrocraqueo de fracciones petroliferas pesadas

Country Status (11)

Country Link
US (1) US5961815A (es)
EP (1) EP0938531A4 (es)
JP (1) JP2001500561A (es)
KR (1) KR100450536B1 (es)
CN (1) CN1079819C (es)
AR (1) AR008190A1 (es)
AU (1) AU714130B2 (es)
BR (1) BR9712097A (es)
CA (1) CA2266460C (es)
RO (1) RO120575B1 (es)
WO (1) WO1998012281A1 (es)

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ES2267520T3 (es) * 1999-06-24 2007-03-16 Catalytic Distillation Technologies Proceso para la desulfuracion de una fraccion de diesel.
US6500309B1 (en) 1999-12-11 2002-12-31 Peter Tung Dimensions in reactive distillation technology
US6547956B1 (en) * 2000-04-20 2003-04-15 Abb Lummus Global Inc. Hydrocracking of vacuum gas and other oils using a post-treatment reactive distillation system
US6867338B2 (en) * 2002-03-15 2005-03-15 Catalytic Distillation Technologies Selective hydrogenation of acetylenes and dienes in a hydrocarbon stream
US7361313B2 (en) * 2003-02-18 2008-04-22 Intel Corporation Methods for uniform metal impregnation into a nanoporous material
US20050035026A1 (en) * 2003-08-14 2005-02-17 Conocophillips Company Catalytic distillation hydroprocessing
US7736490B2 (en) 2003-12-19 2010-06-15 Shell Oil Company Systems, methods, and catalysts for producing a crude product
US7811445B2 (en) 2003-12-19 2010-10-12 Shell Oil Company Systems and methods of producing a crude product
US7745369B2 (en) 2003-12-19 2010-06-29 Shell Oil Company Method and catalyst for producing a crude product with minimal hydrogen uptake
WO2006110660A1 (en) 2005-04-11 2006-10-19 Shell Internationale Research Maatschappij B.V. Method and catalyst for producing a crude product having a reduced mcr content
CN101166811A (zh) 2005-04-11 2008-04-23 国际壳牌研究有限公司 生产具有降低氮含量的原油产品的方法和催化剂
AR058345A1 (es) 2005-12-16 2008-01-30 Petrobeam Inc Craqueo autosostenido en frio de hidrocarburos
US20080087575A1 (en) 2006-10-06 2008-04-17 Bhan Opinder K Systems and methods for producing a crude product and compositions thereof
US7931798B2 (en) * 2008-03-11 2011-04-26 Exxonmobil Research And Engineering Company Hydroconversion process for petroleum resids by hydroconversion over carbon supported metal catalyst followed by selective membrane separation
US7938952B2 (en) * 2008-05-20 2011-05-10 Institute Francais Du Petrole Process for multistage residue hydroconversion integrated with straight-run and conversion gasoils hydroconversion steps
EP2486107A1 (en) * 2009-10-09 2012-08-15 Velocys Inc. Process for treating heavy oil

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US3699036A (en) * 1970-08-21 1972-10-17 Union Oil Co Hydrocracking nitrogen containing feedstocks
US3671420A (en) * 1970-12-24 1972-06-20 Texaco Inc Conversion of heavy petroleum oils
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Also Published As

Publication number Publication date
EP0938531A1 (en) 1999-09-01
KR20000048497A (ko) 2000-07-25
AU4093797A (en) 1998-04-14
AU714130B2 (en) 1999-12-16
BR9712097A (pt) 2000-01-18
CA2266460C (en) 2006-12-12
CN1079819C (zh) 2002-02-27
CA2266460A1 (en) 1998-03-26
RO120575B1 (ro) 2006-04-28
CN1231685A (zh) 1999-10-13
JP2001500561A (ja) 2001-01-16
US5961815A (en) 1999-10-05
WO1998012281A1 (en) 1998-03-26
EP0938531A4 (en) 2000-03-29
KR100450536B1 (ko) 2004-10-01

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