GB837706A - Improvements relating to the catalytic reforming of hydrocarbons - Google Patents

Improvements relating to the catalytic reforming of hydrocarbons

Info

Publication number
GB837706A
GB837706A GB913257A GB913257A GB837706A GB 837706 A GB837706 A GB 837706A GB 913257 A GB913257 A GB 913257A GB 913257 A GB913257 A GB 913257A GB 837706 A GB837706 A GB 837706A
Authority
GB
United Kingdom
Prior art keywords
catalyst
oxide
metal oxide
chromite
reduced
Prior art date
Legal status (The legal status 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 status listed.)
Expired
Application number
GB913257A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BP PLC
Original Assignee
BP PLC
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 to BE568318D priority Critical patent/BE568318A/xx
Application filed by BP PLC filed Critical BP PLC
Priority to GB913257A priority patent/GB837706A/en
Publication of GB837706A publication Critical patent/GB837706A/en
Expired legal-status Critical Current

Links

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
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/86Chromium
    • 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
    • B01J23/90Regeneration or reactivation
    • B01J23/94Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper
    • 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
    • C10G35/00Reforming naphtha
    • C10G35/04Catalytic reforming
    • C10G35/10Catalytic reforming with moving catalysts

Landscapes

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

Abstract

Heat is supplied to an endothermic catalytic reaction employing a fluidized or moving bed of catalyst by including in the catalyst a metal oxide which is reduced with evolution of heat under reaction conditions and using excess oxygen during regeneration to reoxidize reduced metal oxide. The process described is one of dehydrogenation and dehydrocyclization of non-aromatic hydrocarbons (see Group IV (b)) at a temperature of 800-1300 DEG F. employing a chromium oxide-alumina catalyst, the metal oxide added being cupric oxide in an amount of 5-25% by weight of the total catalyst. The catalyst may be promoted with an oxide of a rare earth, bismuth, boron or germanium with or without an alkali metal or a spinal such as cobalt chromite, copper chromite, zinc titanate or iron chromite.ALSO:In an endothermic process for the catalytic dehydrogenation or dehydrocyclization including reforming of hydrocarbon feedstocks containing non-aromatic hydrocarbons employing a fluidized or moving catalyst bed and a reaction temperature of 800-1300 DEG F., heat is supplied by including in the catalyst bed a metal oxide having no appreciable catalytic activity but which is reduced with evolution of heat under the reaction conditions, continuously or intermittently withdrawing catalyst and treating it with oxygen in excess of that required to burn off carbonaceous deposits so that reduced metal oxide is reoxidized and returning regenerated catalyst to the reaction zone. The metal oxide may form an integral part of the catalyst or may be mixed with catalyst particles. Cupric oxide is preferred and may be present in an amount of 5-25% by weight of the total catalyst. This process is preferably applied to the catalytic reforming of petroleum hydrocarbons such as a straight-run light gasoline or a platinum reformate or fraction thereof in the presence of a chromium oxide-alumina catalyst at 840-1075 DEG F., less than 50 p.s.i.g. (including subatmospheric pressures) and a space velocity of 0.1-1.0 vol./vol./hr. without added hydrogen, whether recycle or extraneous. The catalyst may be promoted by an oxide of a rare earth, bismuth, boron or germanium with or without an alkali metal, or a spinel such as cobalt chromite, copper chromite, zinc titanate or iron chromite.
GB913257A 1957-03-20 1957-03-20 Improvements relating to the catalytic reforming of hydrocarbons Expired GB837706A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
BE568318D BE568318A (en) 1957-03-20
GB913257A GB837706A (en) 1957-03-20 1957-03-20 Improvements relating to the catalytic reforming of hydrocarbons

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB913257A GB837706A (en) 1957-03-20 1957-03-20 Improvements relating to the catalytic reforming of hydrocarbons

Publications (1)

Publication Number Publication Date
GB837706A true GB837706A (en) 1960-06-15

Family

ID=9865981

Family Applications (1)

Application Number Title Priority Date Filing Date
GB913257A Expired GB837706A (en) 1957-03-20 1957-03-20 Improvements relating to the catalytic reforming of hydrocarbons

Country Status (2)

Country Link
BE (1) BE568318A (en)
GB (1) GB837706A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016170450A1 (en) * 2015-04-20 2016-10-27 Sabic Global Technologies B.V. Method of improving dehydrogenation of hydrocarbons

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016170450A1 (en) * 2015-04-20 2016-10-27 Sabic Global Technologies B.V. Method of improving dehydrogenation of hydrocarbons

Also Published As

Publication number Publication date
BE568318A (en)

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