NL7210257A - Naphtha reforming - with catalyst having gp 8 noble noble metal supported on refractory oxide contg mordenite - Google Patents

Naphtha reforming - with catalyst having gp 8 noble noble metal supported on refractory oxide contg mordenite

Info

Publication number
NL7210257A
NL7210257A NL7210257A NL7210257A NL7210257A NL 7210257 A NL7210257 A NL 7210257A NL 7210257 A NL7210257 A NL 7210257A NL 7210257 A NL7210257 A NL 7210257A NL 7210257 A NL7210257 A NL 7210257A
Authority
NL
Netherlands
Prior art keywords
catalyst
pref
noble
mordenite
reforming
Prior art date
Application number
NL7210257A
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 filed Critical
Priority to NL7210257A priority Critical patent/NL7210257A/en
Publication of NL7210257A publication Critical patent/NL7210257A/en

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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C10G35/06—Catalytic reforming characterised by the catalyst used
    • C10G35/095—Catalytic reforming characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/18—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the mordenite type
    • B01J29/20—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the mordenite type containing iron group metals, noble metals or copper
    • 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
    • C10G59/00—Treatment 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
    • C10G59/02—Treatment 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 plural serial stages only

Landscapes

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

Abstract

Reforming of an naphtha boiling the range 120-500 degrees F is carried out in the presence of H2 with a catalyst comprising a Gp. 8 noble metal (pref. Pt), mordenite having a SiO2 - to - Al2O3 ratio of >=19:1 (pref. about 27:1) and an absorbent refractory inorganic oxide, pref. gamma- or eta- Al2O3. The feedstock is pref. first contacted with a Pt-Al2O3-halide reforming catalyst. The reforming is pref. carried out at an inlet temp. of 850-1000 degrees F, a press. of 0-1000 psig, a WHSV of >=1 and a recycle gas rate of 3000-10000 SCF/bbl. The process gives a reformate of improved octane no.
NL7210257A 1972-07-25 1972-07-25 Naphtha reforming - with catalyst having gp 8 noble noble metal supported on refractory oxide contg mordenite NL7210257A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
NL7210257A NL7210257A (en) 1972-07-25 1972-07-25 Naphtha reforming - with catalyst having gp 8 noble noble metal supported on refractory oxide contg mordenite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL7210257A NL7210257A (en) 1972-07-25 1972-07-25 Naphtha reforming - with catalyst having gp 8 noble noble metal supported on refractory oxide contg mordenite

Publications (1)

Publication Number Publication Date
NL7210257A true NL7210257A (en) 1974-01-29

Family

ID=19816602

Family Applications (1)

Application Number Title Priority Date Filing Date
NL7210257A NL7210257A (en) 1972-07-25 1972-07-25 Naphtha reforming - with catalyst having gp 8 noble noble metal supported on refractory oxide contg mordenite

Country Status (1)

Country Link
NL (1) NL7210257A (en)

Similar Documents

Publication Publication Date Title
ES8204402A1 (en) Process for the preparation of middle distillates
MY110723A (en) Process for the catalytic partial oxidation of hydrocarbons
NL7210257A (en) Naphtha reforming - with catalyst having gp 8 noble noble metal supported on refractory oxide contg mordenite
NO20003700L (en) Catalyst suitable for the production of hydrogen and carbon monoxide from a hydrocarbon feedstock
GB1286574A (en) Improvements in or relating to catalytic tube assemblies and apparatus employing the same
DE3773695D1 (en) MULTI-ZONE NAPHTHA REFORMING PROCESS.
GB1423889A (en) Catalytic reforming
GB1393592A (en) Combination reforming process
GB1154521A (en) Improvements in and relating to Method for Reforming Hydrogen-Containing Carbonaceous Feedstocks
CA2017658A1 (en) Multizone catalytic reforming process with a plurality of catalysts
ES8205424A1 (en) Startup procedure for reforming catalysts.
FR2265673A1 (en) Sepn of hydrogen from hydrocarbon conversion effluents - by passage through diffusion barriers, and recycling hydrogen
ES8609437A1 (en) Process for catalytic reforming of naphtha using a rhenium-containing catalyst.
FR2145873A5 (en) Benzene from alkylbenzenes
GB1376187A (en) Device for performing catalytic endothermic reactions
GB1452087A (en) Process for regenerating a deactivated reforming catalyst
ES374970A1 (en) Catalytic reforming
GB1433864A (en) Increasing the activity of catalysts containing iridium ruthenium rhodium or osmium
CA868821A (en) Process for the production of gas mixtures for the synthesis of ammonia and methanol, by means of high pressure steam reforming of gaseous and liquid hydrocarbons
GB1293632A (en) Process for regenerating coke-deactivated catalyst
GB1006291A (en) Catalytic conversion of hydrocarbons
GB1254185A (en) Pretreatment of hydroforming feed stock
CA2143893A1 (en) Process for the Hydrocracking of a Hydrocarbonaceous Feedstock
SU681904A1 (en) Process for producing high-octane gasoline
NL7109633A (en) Benzene from alkylbenzenes

Legal Events

Date Code Title Description
BA A request for search or an international-type search has been filed
BB A search report has been drawn up
BV The patent application has lapsed