FR2430973A1 - High-octane gasoline prodn. by hydroisomerisation - using catalyst comprising nickel aluminosilicate and nickel-calcium Y zeolite - Google Patents

High-octane gasoline prodn. by hydroisomerisation - using catalyst comprising nickel aluminosilicate and nickel-calcium Y zeolite

Info

Publication number
FR2430973A1
FR2430973A1 FR7820906A FR7820906A FR2430973A1 FR 2430973 A1 FR2430973 A1 FR 2430973A1 FR 7820906 A FR7820906 A FR 7820906A FR 7820906 A FR7820906 A FR 7820906A FR 2430973 A1 FR2430973 A1 FR 2430973A1
Authority
FR
France
Prior art keywords
degrees
catalyst
nickel
hydroisomerisation
zeolite
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.)
Granted
Application number
FR7820906A
Other languages
French (fr)
Other versions
FR2430973B1 (en
Inventor
M I Ogly Rustamov
V S Aliev
K I Kyzy Abad-Zade
A D Guseinova
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.)
INST NEFTEKHIMICHESKIKH PROT
Original Assignee
INST NEFTEKHIMICHESKIKH PROT
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 INST NEFTEKHIMICHESKIKH PROT filed Critical INST NEFTEKHIMICHESKIKH PROT
Priority to FR7820906A priority Critical patent/FR2430973A1/en
Publication of FR2430973A1 publication Critical patent/FR2430973A1/en
Application granted granted Critical
Publication of FR2430973B1 publication Critical patent/FR2430973B1/fr
Granted legal-status Critical Current

Links

Classifications

    • 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
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/10—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing iron group metals, noble metals or copper
    • B01J29/14—Iron group metals or copper
    • B01J29/146—Y-type faujasite
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline

Abstract

Hydroisomerisation of specified gasoline fraction is carried out a 320-400 degrees C and 20-60 atm. with a space velocity of 1.0-1.5 hr-1 using a catalyst comprising an amorphous Ni aluminosilicate and a NiCaHY zeolite in a wt. ratio of 60-90:40-10. The catalyst contains 7-10 wt.% Ni, 5-6 wt.% Al2O3, 80-86 wt.% SiO2, 1-2 wt.% Ca and 1-2 wt.% H. Specifically, the feed is a straight-run gasoline fraction boiling in the 85-160 degrees C or 160-195 degrees C range or a coker gasoline fraction boiling in the 35-85 degrees C or 43-170 degrees C range (N.B., the used of 35-85 degrees C coker gasoline is not claimed). The process gives high-octane products (MON clear 87-90) useful as motor fuel blending stocks, from low-octane feeds under mild conditions. The catalyst has high activity and stability.
FR7820906A 1978-07-12 1978-07-12 High-octane gasoline prodn. by hydroisomerisation - using catalyst comprising nickel aluminosilicate and nickel-calcium Y zeolite Granted FR2430973A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
FR7820906A FR2430973A1 (en) 1978-07-12 1978-07-12 High-octane gasoline prodn. by hydroisomerisation - using catalyst comprising nickel aluminosilicate and nickel-calcium Y zeolite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7820906A FR2430973A1 (en) 1978-07-12 1978-07-12 High-octane gasoline prodn. by hydroisomerisation - using catalyst comprising nickel aluminosilicate and nickel-calcium Y zeolite

Publications (2)

Publication Number Publication Date
FR2430973A1 true FR2430973A1 (en) 1980-02-08
FR2430973B1 FR2430973B1 (en) 1980-12-12

Family

ID=9210698

Family Applications (1)

Application Number Title Priority Date Filing Date
FR7820906A Granted FR2430973A1 (en) 1978-07-12 1978-07-12 High-octane gasoline prodn. by hydroisomerisation - using catalyst comprising nickel aluminosilicate and nickel-calcium Y zeolite

Country Status (1)

Country Link
FR (1) FR2430973A1 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2145683A1 (en) * 1971-07-14 1973-02-23 Nippon Oil Co Ltd

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2145683A1 (en) * 1971-07-14 1973-02-23 Nippon Oil Co Ltd

Also Published As

Publication number Publication date
FR2430973B1 (en) 1980-12-12

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