GB1083110A - Catalytic conversion of hydrocarbons - Google Patents

Catalytic conversion of hydrocarbons

Info

Publication number
GB1083110A
GB1083110A GB4388465A GB4388465A GB1083110A GB 1083110 A GB1083110 A GB 1083110A GB 4388465 A GB4388465 A GB 4388465A GB 4388465 A GB4388465 A GB 4388465A GB 1083110 A GB1083110 A GB 1083110A
Authority
GB
United Kingdom
Prior art keywords
cracking
compounds
zro2
al2o3
sio2
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
GB4388465A
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.)
Texaco Development Corp
Original Assignee
Texaco Development 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 Texaco Development Corp filed Critical Texaco Development Corp
Publication of GB1083110A publication Critical patent/GB1083110A/en
Expired 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
    • B01J29/061—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing metallic elements added to the zeolite
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other metals or compounds thereof

Landscapes

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

Abstract

A process for cracking a hydrocarbon fraction boiling in the range 400-850 DEG F. comprises use of a catalyst containing (a) nickel, tungsten or compounds thereof; (b) an acidic inorganic oxide in amorphous form selected from SiO2, Al2O3, MgO, ZrO2, or mixtures; and (c) a crystalline zeolite. Typical cracking conditions are: pressure 500-10,000 p.s.i.g.; Hydrogen rate 1000-20,000 SCF/B.; space velocity 0.1-10v./v./hr. Comparative examples describe the cracking of gas oil.ALSO:A hydrocarbon conversion catalyst comprises a crystalline zeolite and an amorphous acidic in-organic oxide of SiO2, Al2O3, MgO, ZrO2 or mixtures which support a metal or compound thereof selected from nickel, tungsten or compounds thereof. Zeolites A, D, X, Y, inordenite, charazite and analcite are specified. Preferred compounds of Ni and W are the oxides and sulphides.
GB4388465A 1964-10-21 1965-10-15 Catalytic conversion of hydrocarbons Expired GB1083110A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US40560264A 1964-10-21 1964-10-21

Publications (1)

Publication Number Publication Date
GB1083110A true GB1083110A (en) 1967-09-13

Family

ID=23604374

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4388465A Expired GB1083110A (en) 1964-10-21 1965-10-15 Catalytic conversion of hydrocarbons

Country Status (2)

Country Link
DE (1) DE1545399A1 (en)
GB (1) GB1083110A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1645711A1 (en) * 1968-02-17 1970-05-14 Basf Ag Process for the hydrogenative cracking of hydrocarbons
WO2008005975A2 (en) * 2006-07-06 2008-01-10 Shell Oil Company Process for making an improved isomerization catalyst

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1645711A1 (en) * 1968-02-17 1970-05-14 Basf Ag Process for the hydrogenative cracking of hydrocarbons
WO2008005975A2 (en) * 2006-07-06 2008-01-10 Shell Oil Company Process for making an improved isomerization catalyst
WO2008005975A3 (en) * 2006-07-06 2008-02-21 Shell Oil Co Process for making an improved isomerization catalyst

Also Published As

Publication number Publication date
DE1545399A1 (en) 1969-12-11

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