GB563647A - An improved process for the pyrolitic conversion of hydrocarbons - Google Patents
An improved process for the pyrolitic conversion of hydrocarbonsInfo
- Publication number
- GB563647A GB563647A GB10057/42A GB1005742A GB563647A GB 563647 A GB563647 A GB 563647A GB 10057/42 A GB10057/42 A GB 10057/42A GB 1005742 A GB1005742 A GB 1005742A GB 563647 A GB563647 A GB 563647A
- Authority
- GB
- United Kingdom
- Prior art keywords
- oil
- line
- coil
- steam
- gasoline
- 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
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
563,647. Cracking oils. STANDARD OIL DEVELOPMENT CO. July 20, 1942, No. 10057. Convention date, July 24, 1941. [Class 32] Gasoline of high octane value and coke are produced from crude petroleum oils by preheating the oil to about 500-700‹ F. and discharging it into a coking zone into which gases, e.g. steam, carbon dioxide, flue gas, gaseous hydrocarbons heated to 1500-1800‹ F. are discharged, the oil being maintained in the coking zone for about 10-15 seconds, while the vaporized hydrocarbons are withdrawn and fractionated in known manner to yield gasoline and gas oil. Crude oil from tank 1 is preheated in coil 5 and passed into the top of coking drum 10 to which superheated steam obtained by passing water from a drum 30 through a coil 40, is admitted through line 45. The vapours formed pass off through line 12 to a fractionating tower 14 from which gaseous hydrocarbons are taken off through line 16, gasoline through line 18, and gas oil at the bottom of the tower through line 19 ; the latter may be recycled to the coil 5. In treating a reduced Texas crude, the following conditions are specified : (a) coking drum pressures of 15 lbs. per sq. inch ; (b) steam inlet temperature' of 1500‹ F. ; (c) oil inlet temperature of 800‹ F. ; (d) lbs. steam per gallon oil-18.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US563647XA | 1941-07-24 | 1941-07-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB563647A true GB563647A (en) | 1944-08-24 |
Family
ID=22003904
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10057/42A Expired GB563647A (en) | 1941-07-24 | 1942-07-20 | An improved process for the pyrolitic conversion of hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB563647A (en) |
-
1942
- 1942-07-20 GB GB10057/42A patent/GB563647A/en not_active Expired
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