AR000314A1 - Hydrocarbon conversion procedures including catalytic hydrocracking - Google Patents

Hydrocarbon conversion procedures including catalytic hydrocracking

Info

Publication number
AR000314A1
AR000314A1 AR33455895A AR33455895A AR000314A1 AR 000314 A1 AR000314 A1 AR 000314A1 AR 33455895 A AR33455895 A AR 33455895A AR 33455895 A AR33455895 A AR 33455895A AR 000314 A1 AR000314 A1 AR 000314A1
Authority
AR
Argentina
Prior art keywords
boiling point
atmospheric boiling
hydrocracked
hydrocarbon conversion
procedures including
Prior art date
Application number
AR33455895A
Other languages
Spanish (es)
Inventor
Bharne Gurunath Ganapat
Tom Huizinga
Original Assignee
Shell Int Research
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
Priority claimed from GBGB9504515.9A external-priority patent/GB9504515D0/en
Application filed by Shell Int Research filed Critical Shell Int Research
Publication of AR000314A1 publication Critical patent/AR000314A1/en

Links

Classifications

    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)

Abstract

La presente invención brinda un procedimiento para convertir una carga de alimentación hidrocarbúrica (1) en materiales de ebullición inferior quecomprende los pasos de: (a) poner en contacto una carga de alimentación (1), a una temperaturaelev ada y a una presión elevada, con hidrógeno en presenciade un catalizador de hidrocraqueo A para formar un producto hidrocraqueado (3); (b) separar como mínimo una parte del producto hidrocraqueado (3) del paso (a)por medio de destilación en porlo me nos un destilado hidrocraqueado (7) que posee un 5% de punto de ebullición atmosférico de >/= 0°C y un 95% de puntode ebullición atmosférico de </= 160°C, y por lo menos un destilado hidrocraqueado (8, 9, 10) que posea un 95% depunto de ebullición atmosféricode >/= 200°C; y (c) poner en contacto como mínimo una parte de por lo menos un destilado hidrocraqueado (7)que posea un 5% de punto de ebulliciónatmosférico de >/= 0°C y un 95% de punto de ebullición atmosférico de</= 16 0°C a una temperatura elevada y a una presión elevada, con hidrógeno en presenciade un catalizador de hidrocraqueo B que comprenda un tamiz molecular.The present invention provides a method of converting a hydrocarbon feed charge (1) to lower boiling materials comprising the steps of: (a) bringing a feed charge (1) into contact at elevated temperature and elevated pressure, with hydrogen in the presence of a hydrocracking catalyst A to form a hydrocracked product (3); (b) separating at least a part of the hydrocracked product (3) from step (a) by means of distillation, therefore at least one hydrocracked distillate (7) that has a 5% atmospheric boiling point of> / = 0 ° C and 95% atmospheric boiling point of </ = 160 ° C, and at least one hydrocracked distillate (8, 9, 10) having 95% atmospheric boiling point of> / = 200 ° C; and (c) contacting at least a part of at least one hydrocracked distillate (7) that has a 5% atmospheric boiling point of> / = 0 ° C and a 95% atmospheric boiling point of </ = 16 0 ° C at elevated temperature and at elevated pressure, with hydrogen in the presence of a hydrocracking catalyst B comprising a molecular sieve.

AR33455895A 1994-12-13 1995-12-11 Hydrocarbon conversion procedures including catalytic hydrocracking AR000314A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP94203627 1994-12-13
GBGB9504515.9A GB9504515D0 (en) 1995-03-07 1995-03-07 Hydrocarbon conversion process

Publications (1)

Publication Number Publication Date
AR000314A1 true AR000314A1 (en) 1997-06-18

Family

ID=26136810

Family Applications (1)

Application Number Title Priority Date Filing Date
AR33455895A AR000314A1 (en) 1994-12-13 1995-12-11 Hydrocarbon conversion procedures including catalytic hydrocracking

Country Status (3)

Country Link
JP (1) JPH08283748A (en)
CN (1) CN1050626C (en)
AR (1) AR000314A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AR032930A1 (en) * 2001-03-05 2003-12-03 Shell Int Research PROCEDURE TO PREPARE AN OIL BASED OIL AND GAS OIL
CN101035881B (en) * 2004-09-08 2010-10-13 国际壳牌研究有限公司 Hydrocracking catalyst composition
JP4925653B2 (en) * 2005-11-30 2012-05-09 Ｊｘ日鉱日石エネルギー株式会社 Method for producing liquefied fuel gas composition

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4401556A (en) * 1979-11-13 1983-08-30 Union Carbide Corporation Midbarrel hydrocracking
FR2563445B1 (en) * 1984-04-26 1986-08-14 Pro Catalyse Ste Fse Prod Cata NEW HYDROCRACKING CATALYST FOR THE PRODUCTION OF MEDIUM DISTILLATES
GB8613131D0 (en) * 1986-05-30 1986-07-02 Shell Int Research Hydrocarbon conversion
AT392810B (en) * 1989-04-18 1991-06-25 Plasser Bahnbaumasch Franz MOBILE TRACKING MACHINE WITH CROSS- AND HEIGHT-ADJUSTABLE STOPPING UNITS

Also Published As

Publication number Publication date
CN1131693A (en) 1996-09-25
JPH08283748A (en) 1996-10-29
CN1050626C (en) 2000-03-22

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