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 oilsInfo
- 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
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.
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)
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 |
-
1925
- 1925-04-17 GB GB1009225A patent/GB255159A/en not_active Expired
Cited By (9)
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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