GB254011A - Process of and apparatus for the conversion of crude mineral or shale oil or tar oils into light oil or spirit and for the preparation of light oil or spirit from coal, l ignite or other carbonaceous material - Google Patents

Process of and apparatus for the conversion of crude mineral or shale oil or tar oils into light oil or spirit and for the preparation of light oil or spirit from coal, l ignite or other carbonaceous material

Info

Publication number
GB254011A
GB254011A GB806225A GB806225A GB254011A GB 254011 A GB254011 A GB 254011A GB 806225 A GB806225 A GB 806225A GB 806225 A GB806225 A GB 806225A GB 254011 A GB254011 A GB 254011A
Authority
GB
United Kingdom
Prior art keywords
spirit
cylinder
light oil
vapours
oil
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
GB806225A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to GB806225A priority Critical patent/GB254011A/en
Publication of GB254011A publication Critical patent/GB254011A/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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Working-Up Tar And Pitch (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

254,011. Schultz, A. March 25, 1925. Purifying oils.-Vapours from an oil still z or from an apparatus of the kind described in Specification 252,422, [Class 55 (i), Coking &c.], for distilling coal lignite or other carbonaceous material are treated to give a greater yield of low-boiling oils or spirit by passing them through a converter maintained at a lower temperature than the still or retort and containing lime together with zinc, zinc oxide or chloride, aluminium chloride., bauxite, magnesia, common salt, charcoal, coke, &c. The condensate is purified by acid and alkali treatment. The converter may be a vertical cylinder containing the materials on trays or holders, fitted with agitating blades and heated by the passage of the vapours. Alternatively a horizontal cylinder 7 heated by a separate furnace a may be used. The cylinder 7 is divided by partitions between which are screw plates carried by a central rotary shaft. The converting-materials may be passed continuously through the cylinder from an inlet hopper 12 to an outlet valve at the opposite end. If the vapours contain phenols or cresols, the inner surface of the converting chamber is tinned.
GB806225A 1925-03-25 1925-03-25 Process of and apparatus for the conversion of crude mineral or shale oil or tar oils into light oil or spirit and for the preparation of light oil or spirit from coal, l ignite or other carbonaceous material Expired GB254011A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB806225A GB254011A (en) 1925-03-25 1925-03-25 Process of and apparatus for the conversion of crude mineral or shale oil or tar oils into light oil or spirit and for the preparation of light oil or spirit from coal, l ignite or other carbonaceous material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB806225A GB254011A (en) 1925-03-25 1925-03-25 Process of and apparatus for the conversion of crude mineral or shale oil or tar oils into light oil or spirit and for the preparation of light oil or spirit from coal, l ignite or other carbonaceous material

Publications (1)

Publication Number Publication Date
GB254011A true GB254011A (en) 1926-06-25

Family

ID=9845037

Family Applications (1)

Application Number Title Priority Date Filing Date
GB806225A Expired GB254011A (en) 1925-03-25 1925-03-25 Process of and apparatus for the conversion of crude mineral or shale oil or tar oils into light oil or spirit and for the preparation of light oil or spirit from coal, l ignite or other carbonaceous material

Country Status (1)

Country Link
GB (1) GB254011A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2419507A (en) * 1940-10-16 1947-04-22 Socony Vacuum Oil Co Inc Method of catalytic conversion
US2419508A (en) * 1941-10-01 1947-04-22 Socony Vacuum Oil Co Inc Apparatus for catalytic conversion
US2441666A (en) * 1939-12-09 1948-05-18 Standard Oil Dev Co Powdered catalyst process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2441666A (en) * 1939-12-09 1948-05-18 Standard Oil Dev Co Powdered catalyst process
US2419507A (en) * 1940-10-16 1947-04-22 Socony Vacuum Oil Co Inc Method of catalytic conversion
US2419508A (en) * 1941-10-01 1947-04-22 Socony Vacuum Oil Co Inc Apparatus for catalytic conversion

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