GB1037581A - Hydrocracking process - Google Patents

Hydrocracking process

Info

Publication number
GB1037581A
GB1037581A GB1105064A GB1105064A GB1037581A GB 1037581 A GB1037581 A GB 1037581A GB 1105064 A GB1105064 A GB 1105064A GB 1105064 A GB1105064 A GB 1105064A GB 1037581 A GB1037581 A GB 1037581A
Authority
GB
United Kingdom
Prior art keywords
hydrogen
nitrogen
produce
per mole
millimoles
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
GB1105064A
Inventor
Paul Francis Helfrey
Nicholas Leo Kay
Bernal Peralta
Cloyd Pritchard Reeg
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.)
Union Oil Company of California
Original Assignee
Union Oil Company of California
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 Union Oil Company of California filed Critical Union Oil Company of California
Priority to GB1105064A priority Critical patent/GB1037581A/en
Publication of GB1037581A publication Critical patent/GB1037581A/en
Expired legal-status Critical Current

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
    • 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
    • C10G47/18—Crystalline alumino-silicate carriers the catalyst containing platinum group metals or compounds thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00—Engines characterised by air compression and subsequent fuel addition
    • F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition

Landscapes

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

Abstract

Hydrocarbon feedstocks boiling above the gasoline range, free of nitrogen and containing at least 20% by volume of aromatics are hydrocracked at 400-2500 p.s.i.g., and 400-750 DEG F. in the presence of a catalyst containing a Group 8 noble metal and in the presence of hydrogen sulphide; in one variant there is present more than 0-01 (preferably more than 0.2) millimoles of hydrogen sulphide per mole of hydrogen to produce a relatively aromatic gasoline and in another less than 0-2 millimoles per mole to produce a relatively non-aromatic jet or diesel fuel and the concentration may be varied from time to time according to the product desired. The feed should contain less than 50 p.p.m. of nitrogen but may contain sulphur. The LHSV may be 0-5-10 and 500-20,000 SCF/B of hydrogen are used. The metal catalyst may be supported on silica composites or molecular sieves.
GB1105064A 1964-03-16 1964-03-16 Hydrocracking process Expired GB1037581A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1105064A GB1037581A (en) 1964-03-16 1964-03-16 Hydrocracking process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1105064A GB1037581A (en) 1964-03-16 1964-03-16 Hydrocracking process

Publications (1)

Publication Number Publication Date
GB1037581A true GB1037581A (en) 1966-07-27

Family

ID=9979091

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1105064A Expired GB1037581A (en) 1964-03-16 1964-03-16 Hydrocracking process

Country Status (1)

Country Link
GB (1) GB1037581A (en)

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