SE327393B - - Google Patents

Info

Publication number
SE327393B
SE327393B SE01752/67A SE175267A SE327393B SE 327393 B SE327393 B SE 327393B SE 01752/67 A SE01752/67 A SE 01752/67A SE 175267 A SE175267 A SE 175267A SE 327393 B SE327393 B SE 327393B
Authority
SE
Sweden
Prior art keywords
catalyst
see division
aluminosilicate
ions
dealkylation
Prior art date
Application number
SE01752/67A
Inventor
C Plank
E Rosinski
Original Assignee
Mobil Oil Corp
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 Mobil Oil Corp filed Critical Mobil Oil Corp
Publication of SE327393B publication Critical patent/SE327393B/xx

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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • 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
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves

Landscapes

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

Abstract

A process for hydrocarbon conversion uses as catalyst a crystalline aluminosilicate having a silica/alumina ratio in excess of 3 and uniform pores between 6 and 15 <\>rA in diameter and containing cations below sodium in the electromotive series, or calcium, or any mixtures thereof, ammonium, hydrogen or organic nitrogen base ions, and less than 3% of alkali metal ions (see Division C1). The aluminosilicate may be suspended in and distributed throughout a matrix of a binding agent, and the composition may also contain an additive to increase its porosity (see Division B1). The cracking of a mid-Continent gas oil having a boiling range 450-950 DEG F. to gasoline having an end boiling point of 410 DEG F. at atmospheric pressure and at 875-900 DEG F. using various catalysts according to the invention is described The catalyst may also be used in alkylation, dealkylation, disproportionation, isomerization and polymerization reactions.
SE01752/67A 1962-05-17 1967-02-08 SE327393B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US19543062A 1962-05-17 1962-05-17
US19594562A 1962-05-18 1962-05-18
US20267762A 1962-06-15 1962-06-15

Publications (1)

Publication Number Publication Date
SE327393B true SE327393B (en) 1970-08-24

Family

ID=27393448

Family Applications (2)

Application Number Title Priority Date Filing Date
SE549463A SE324351B (en) 1962-05-17 1963-05-17
SE01752/67A SE327393B (en) 1962-05-17 1967-02-08

Family Applications Before (1)

Application Number Title Priority Date Filing Date
SE549463A SE324351B (en) 1962-05-17 1963-05-17

Country Status (5)

Country Link
CH (3) CH421910A (en)
DE (1) DE1442853C3 (en)
GB (3) GB1049891A (en)
NO (1) NO115009B (en)
SE (2) SE324351B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ZA735587B (en) * 1972-08-21 1974-07-31 Universal Oil Prod Co Catalyst and method of manufacture
US3994800A (en) * 1975-02-19 1976-11-30 W. R. Grace & Co. Catalytic cracking with catalyst of improved Y zeolite
DE2617571A1 (en) * 1975-04-24 1976-11-11 Grace W R & Co PROCESS FOR MANUFACTURING ZEOLITHES WITH HIGH SILICON OXIDE-ALUMINUM OXIDE RATIO
KR100200612B1 (en) * 1996-07-31 1999-06-15 윤종용 Method for manufacturing porous composite oxide

Also Published As

Publication number Publication date
DE1442853C3 (en) 1980-08-14
GB1049891A (en) 1966-11-30
GB1049892A (en) 1966-11-30
GB1049893A (en) 1966-11-30
SE324351B (en) 1970-06-01
CH421910A (en) 1966-10-15
DE1442853B2 (en) 1979-11-15
DE1442853A1 (en) 1969-06-19
NO115009B (en) 1968-07-01
CH476094A (en) 1969-07-31
CH466235A (en) 1968-12-15

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