GB255159A - Improvements in or relating to the cracking and hydrogenation of hydrocarbon oils - Google Patents

Improvements in or relating to the cracking and hydrogenation of hydrocarbon oils

Info

Publication number
GB255159A
GB255159A GB1009225A GB1009225A GB255159A GB 255159 A GB255159 A GB 255159A GB 1009225 A GB1009225 A GB 1009225A GB 1009225 A GB1009225 A GB 1009225A GB 255159 A GB255159 A GB 255159A
Authority
GB
United Kingdom
Prior art keywords
chamber
pipe
combustion
supplied
hydrogenation
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
GB1009225A
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 GB1009225A priority Critical patent/GB255159A/en
Publication of GB255159A publication Critical patent/GB255159A/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
    • 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

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)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

255,159. Wallace, G. W. April 17, 1925. Hydrocarbons, cracking; hydrogenation, destructive.-Hydrocarbon oils are cracked by vaporizing them in a chamber and passing the vapours in countercurrent through a heated inert material such as carbon briquettes or pieces of carbon, firebrick, alumina, &c. which is impelled mechanically through the chamber. The material may be coated or treated with a catalyst such as nickel and, if hydrogenation is desired, hydrogen or steam may be passed with the vapours. The chamber 1 which may be horizontal or inclined is supplied with the inert material from a hopper 6 by a piston 4 or by a screw conveyer, which discharges the material into a second chamber 1<b>. Oil is supplied through a nozzle 11 or a pipe 9 and vapours are withdrawn through a pipe 8. The chamber 1 is heated externally or by passage through it of products of combustion from a surface-combustion burner of the kind described in Specification 233,395 attached to the opening 12 or by partial combustion of the oil supplied to the nozzle 11 or by combustion of residual products &c. in the materials in the chamber 1<b> by air, steam, or gas supplied by a pipe 15. The inert material may be broken up by rollers 14 and quenched by water from a pipe 21 prior to being discharged and returned to the hopper 6. Gases formed in the chamber 1<b> by action of air and steam on the residual materials may either pass through the chamber 1 or may be withdrawn through an outlet 19 and used heating purposes.
GB1009225A 1925-04-17 1925-04-17 Improvements in or relating to the cracking and hydrogenation of hydrocarbon oils Expired GB255159A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1009225A GB255159A (en) 1925-04-17 1925-04-17 Improvements in or relating to the cracking and hydrogenation of hydrocarbon oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1009225A GB255159A (en) 1925-04-17 1925-04-17 Improvements in or relating to the cracking and hydrogenation of hydrocarbon oils

Publications (1)

Publication Number Publication Date
GB255159A true GB255159A (en) 1926-07-19

Family

ID=9961321

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1009225A Expired GB255159A (en) 1925-04-17 1925-04-17 Improvements in or relating to the cracking and hydrogenation of hydrocarbon oils

Country Status (1)

Country Link
GB (1) GB255159A (en)

Cited By (9)

* 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
US2422790A (en) * 1940-12-19 1947-06-24 Socony Vacuum Oil Co Inc Method of coking oils
US2431462A (en) * 1942-11-17 1947-11-25 Standard Oil Dev Co Catalytic treatment of hydrocarbons
US2433079A (en) * 1939-09-30 1947-12-23 Standard Oil Dev Co Catalytic isomerization process
US2433798A (en) * 1940-07-31 1947-12-30 Standard Oil Co Catalytic hydrocarbon conversion process and apparatus therefor
US2485315A (en) * 1947-12-06 1949-10-18 Standard Oil Dev Co Controlled severity fluid coking
US2574503A (en) * 1946-02-12 1951-11-13 Socony Vacuum Oil Co Inc Method and apparatus for hydrocarbon conversion
US2612364A (en) * 1949-01-28 1952-09-30 Fmc Corp Regenerative furnace of the pebble bed type

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2433079A (en) * 1939-09-30 1947-12-23 Standard Oil Dev Co Catalytic isomerization process
US2433798A (en) * 1940-07-31 1947-12-30 Standard Oil Co Catalytic hydrocarbon conversion process and apparatus therefor
US2419507A (en) * 1940-10-16 1947-04-22 Socony Vacuum Oil Co Inc Method of catalytic conversion
US2422790A (en) * 1940-12-19 1947-06-24 Socony Vacuum Oil Co Inc Method of coking oils
US2419508A (en) * 1941-10-01 1947-04-22 Socony Vacuum Oil Co Inc Apparatus for catalytic conversion
US2431462A (en) * 1942-11-17 1947-11-25 Standard Oil Dev Co Catalytic treatment of hydrocarbons
US2574503A (en) * 1946-02-12 1951-11-13 Socony Vacuum Oil Co Inc Method and apparatus for hydrocarbon conversion
US2485315A (en) * 1947-12-06 1949-10-18 Standard Oil Dev Co Controlled severity fluid coking
US2612364A (en) * 1949-01-28 1952-09-30 Fmc Corp Regenerative furnace of the pebble bed type

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