WO2002000578A3 - Conversion of refinery c5 paraffins into c4 and c6 paraffins - Google Patents

Conversion of refinery c5 paraffins into c4 and c6 paraffins Download PDF

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Publication number
WO2002000578A3
WO2002000578A3 PCT/US2001/019697 US0119697W WO0200578A3 WO 2002000578 A3 WO2002000578 A3 WO 2002000578A3 US 0119697 W US0119697 W US 0119697W WO 0200578 A3 WO0200578 A3 WO 0200578A3
Authority
WO
WIPO (PCT)
Prior art keywords
paraffins
fraction
product stream
olefins
catalyst
Prior art date
Application number
PCT/US2001/019697
Other languages
French (fr)
Other versions
WO2002000578A2 (en
Inventor
Cong-Yan Chen
Dennis J O'rear
Scott R Brundage
Original Assignee
Chevron Usa Inc
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 Chevron Usa Inc filed Critical Chevron Usa Inc
Priority to AU2001268605A priority Critical patent/AU2001268605A1/en
Publication of WO2002000578A2 publication Critical patent/WO2002000578A2/en
Publication of WO2002000578A3 publication Critical patent/WO2002000578A3/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/64Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652Chromium, molybdenum or tungsten
    • B01J23/6527Tungsten
    • B01J35/19
    • 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
    • C10G45/00Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • 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
    • C10G59/00Treatment of naphtha by two or more reforming processes only or by at least one reforming process and at least one process which does not substantially change the boiling range of the naphtha
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/582Recycling of unreacted starting or intermediate materials

Abstract

A process for preparing a C4- product stream and a C¿6+? product stream is disclosed. The process involves contacting a C5 containing paraffinic feedstock with a catalyst that includes a hydrogenation/dehydrogenation catalyst and an olefin metathesis catalyst under conditions which dehydrogenate the paraffins to olefins. The olefins are then metathesized and rehydrogenated to provide a product stream. A C4- fraction a C6+ fraction can each be isolated from the product stream. The C4- fraction can be used, for example, in an alkylation reaction to provide compounds useful in gasoline compositions. Unconverted C5 paraffins can be recycled. The C6+ fraction can be used, for example, as solvents. Alternatively, they can be isomerized to form gasoline additives, or can be converted to aromatic compounds via reforming, for example, using conventional reforming techniques, preferably using the AROMAX?TM¿ process or traditional rheniforming conditions.
PCT/US2001/019697 2000-06-23 2001-06-19 Conversion of refinery c5 paraffins into c4 and c6 paraffins WO2002000578A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2001268605A AU2001268605A1 (en) 2000-06-23 2001-06-19 Conversion of refinery c5 paraffins into c4 and c6 paraffins

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/603,489 US6566569B1 (en) 2000-06-23 2000-06-23 Conversion of refinery C5 paraffins into C4 and C6 paraffins
US09/603,489 2000-06-23

Publications (2)

Publication Number Publication Date
WO2002000578A2 WO2002000578A2 (en) 2002-01-03
WO2002000578A3 true WO2002000578A3 (en) 2002-05-02

Family

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Family Applications (1)

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PCT/US2001/019697 WO2002000578A2 (en) 2000-06-23 2001-06-19 Conversion of refinery c5 paraffins into c4 and c6 paraffins

Country Status (3)

Country Link
US (1) US6566569B1 (en)
AU (1) AU2001268605A1 (en)
WO (1) WO2002000578A2 (en)

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CN109529925A (en) * 2018-11-12 2019-03-29 山东科技大学 Load Performance of Isomerization Catalysts for Light n-Paraffin, preparation method and its application method of molybdenum boride
US11198822B2 (en) 2019-04-10 2021-12-14 Exxonmobil Research And Engineering Company Processes to convert naphtha to heavier products
US10975314B2 (en) * 2019-04-24 2021-04-13 Phillips 66 Company Isomerization, catalytic activation and alkylation of pentane-enriched hydrocarbon mixtures
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US6566569B1 (en) 2003-05-20
WO2002000578A2 (en) 2002-01-03
AU2001268605A1 (en) 2002-01-08

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