GB785312A - Improvements relating to hydrocatalytic desulphurisation processes - Google Patents

Improvements relating to hydrocatalytic desulphurisation processes

Info

Publication number
GB785312A
GB785312A GB3552654A GB3552654A GB785312A GB 785312 A GB785312 A GB 785312A GB 3552654 A GB3552654 A GB 3552654A GB 3552654 A GB3552654 A GB 3552654A GB 785312 A GB785312 A GB 785312A
Authority
GB
United Kingdom
Prior art keywords
catalyst
fluorine
regenerated
consisting essentially
fluoride
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
GB3552654A
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.)
FREDERICK WILLIAM BERTRAM PORT
BP PLC
Original Assignee
FREDERICK WILLIAM BERTRAM PORT
BP PLC
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
Priority to BE543447D priority Critical patent/BE543447A/xx
Priority to DENDAT1071258D priority patent/DE1071258B/de
Application filed by FREDERICK WILLIAM BERTRAM PORT, BP PLC filed Critical FREDERICK WILLIAM BERTRAM PORT
Priority to GB3552654A priority patent/GB785312A/en
Priority to FR1143211D priority patent/FR1143211A/en
Publication of GB785312A publication Critical patent/GB785312A/en
Expired legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B60—VEHICLES IN GENERAL
    • B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
    • B60C9/00—Reinforcements or ply arrangement of pneumatic tyres
    • B60C9/0042—Reinforcements made of synthetic materials
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/24—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing with hydrogen-generating compounds
    • C10G45/28—Organic compounds; Autofining

Landscapes

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

Abstract

Petroleum hydrocarbons are autofined using a fluidized bed of a catalyst consisting essentially of the oxides of cobalt and molybdenum incorporated with a support consisting essentially of activated alumina, and containing 0.1-6 per cent of combined fluorine; catalyst is regenerated, for example by burning in air at 1050 DEG F., fluorine lost by this treatment being made up by addition of butyl fluoride to the headstock, and returned to the reaction zone. The catalyst may be regenerated continuously, or a part of the catalyst may be regenerated periodically. The autofining temperature may be 700 DEG to 800 DEG F. and the pressure may be allowed to reach equilibrium. The fluorine may be added to the catalyst in the form of tertiary butyl fluoride or aluminium fluoride. Specifications 654,152, 663,038, 669,536, 669,552, 669,553, 679,175, 697,083, 697,222, 297,226 and 719,627 are referred to.
GB3552654A 1954-12-08 1954-12-08 Improvements relating to hydrocatalytic desulphurisation processes Expired GB785312A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
BE543447D BE543447A (en) 1954-12-08
DENDAT1071258D DE1071258B (en) 1954-12-08
GB3552654A GB785312A (en) 1954-12-08 1954-12-08 Improvements relating to hydrocatalytic desulphurisation processes
FR1143211D FR1143211A (en) 1954-12-08 1955-12-05 Self-refining process for petroleum hydrocarbons

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3552654A GB785312A (en) 1954-12-08 1954-12-08 Improvements relating to hydrocatalytic desulphurisation processes

Publications (1)

Publication Number Publication Date
GB785312A true GB785312A (en) 1957-10-23

Family

ID=10378718

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3552654A Expired GB785312A (en) 1954-12-08 1954-12-08 Improvements relating to hydrocatalytic desulphurisation processes

Country Status (4)

Country Link
BE (1) BE543447A (en)
DE (1) DE1071258B (en)
FR (1) FR1143211A (en)
GB (1) GB785312A (en)

Also Published As

Publication number Publication date
FR1143211A (en) 1957-09-27
BE543447A (en)
DE1071258B (en) 1959-12-17

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