NO20091789L - Fremgangsmate for fremstilling av et raoljeprodukt - Google Patents

Fremgangsmate for fremstilling av et raoljeprodukt

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Publication number
NO20091789L
NO20091789L NO20091789A NO20091789A NO20091789L NO 20091789 L NO20091789 L NO 20091789L NO 20091789 A NO20091789 A NO 20091789A NO 20091789 A NO20091789 A NO 20091789A NO 20091789 L NO20091789 L NO 20091789L
Authority
NO
Norway
Prior art keywords
crude oil
oil product
catalysts
preparation
residual content
Prior art date
Application number
NO20091789A
Other languages
English (en)
Inventor
Scott Lee Wellington
Opinder Kishan Bhan
Original Assignee
Shell Int Research
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Filing date
Publication date
Application filed by Shell Int Research filed Critical Shell Int Research
Publication of NO20091789L publication Critical patent/NO20091789L/no

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    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
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    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
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    • C10G2300/302Viscosity
    • 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
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/30Physical properties of feedstocks or products
    • C10G2300/308Gravity, density, e.g. API
    • 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
    • C10G2300/4006Temperature
    • 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
    • C10G2300/4012Pressure
    • 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
    • C10G2300/4018Spatial velocity, e.g. LHSV, WHSV

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

Abstract

Systemer, fremgangsmåter og katalysatorer for omdannelse av en hydrokarbontilførsel til et totalprodukt beskrives. Ved å bringe hydrokarbontilførselen i kontakt med en eller flere katalysatorer produseres totalproduktet. Dette innbefatter et råoljeprodukt som er en flytende blanding ved 25 °C og 0,101 MPa og som har et residuinnhold på høyst 90 % av residuinnholdet i hydrokarbontilførselen. Minst en av katalysatorene omfatter et metall fra kolonne 6 i det periodiske system, finoppdelt mineraloksid og en bærer.
NO20091789A 2006-10-06 2009-05-05 Fremgangsmate for fremstilling av et raoljeprodukt NO20091789L (no)

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BRPI0717298A2 (pt) 2014-04-29
KR20090085607A (ko) 2009-08-07
CN101534940A (zh) 2009-09-16
RU2448152C2 (ru) 2012-04-20
RU2009117176A (ru) 2010-11-20
KR20090102735A (ko) 2009-09-30
US20080135449A1 (en) 2008-06-12
CA2665479A1 (en) 2008-05-22
CA2665560A1 (en) 2008-04-17
EP2073926A2 (en) 2009-07-01
US20080087578A1 (en) 2008-04-17
JP2010506011A (ja) 2010-02-25
KR20090085606A (ko) 2009-08-07
BRPI0717780A2 (pt) 2014-04-22
US20080083650A1 (en) 2008-04-10
CN101534939A (zh) 2009-09-16
BRPI0717781A2 (pt) 2014-09-16
WO2008045758A1 (en) 2008-04-17
BRPI0717467A2 (pt) 2014-07-08
US7749374B2 (en) 2010-07-06
KR101547526B1 (ko) 2015-08-26
JP2014012845A (ja) 2014-01-23
BRPI0717467B1 (pt) 2017-12-26
WO2008045760A1 (en) 2008-04-17
CA2665631C (en) 2016-06-21
RU2474607C2 (ru) 2013-02-10
KR20090106455A (ko) 2009-10-09
US20080083655A1 (en) 2008-04-10
EP2073927A1 (en) 2009-07-01
CN101535449A (zh) 2009-09-16
CA2665373A1 (en) 2008-04-17
CN101583422A (zh) 2009-11-18
US20080087575A1 (en) 2008-04-17
KR20090102737A (ko) 2009-09-30
JP2010506012A (ja) 2010-02-25
EP2073925A2 (en) 2009-07-01
CN101535448A (zh) 2009-09-16
BRPI0717482A2 (pt) 2014-04-08
WO2008045749A3 (en) 2008-05-29
US20080085225A1 (en) 2008-04-10
WO2008045750A2 (en) 2008-04-17
WO2008045750A3 (en) 2009-04-23
WO2008045757A3 (en) 2008-05-29
RU2009117168A (ru) 2010-11-20
BRPI0717478A2 (pt) 2014-06-24
CA2665545A1 (en) 2008-04-17
EP2073924A2 (en) 2009-07-01
CN101541421A (zh) 2009-09-23
CA2665631A1 (en) 2008-04-17
WO2008045749A2 (en) 2008-04-17
KR20090102736A (ko) 2009-09-30
US20090188836A1 (en) 2009-07-30
NO20091790L (no) 2009-07-03
BRPI0717480A2 (pt) 2014-04-08

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