GB277983A - - Google Patents
Info
- Publication number
- GB277983A GB277983A GB25033/27A GB2503327A GB277983A GB 277983 A GB277983 A GB 277983A GB 25033/27 A GB25033/27 A GB 25033/27A GB 2503327 A GB2503327 A GB 2503327A GB 277983 A GB277983 A GB 277983A
- Authority
- GB
- United Kingdom
- Prior art keywords
- pipe
- cracking
- coil
- passed
- temperature
- 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
- C10G9/00—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G9/14—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils in pipes or coils with or without auxiliary means, e.g. digesters, soaking drums, expansion means
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (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
277,983. Perelis, W. J. Sept. 23, 1926, [Convention date]. Grant of Patent opposed. Hydrocarbons, cracking. - In a process for cracking oils of the tube and drum type the oil while at cracking temperature is agitated either by passing it through a tubular cooling apparatus under conditions of turbulent flow or by mechanical agitation. The raw material is deprived of its volatile fractions by passage through heat exchangers 20, 16 and then flows to a container 33 from which it is pumped by a pump Z through cracking coils 61, 71. 81, the temperature being kept lower in the coil 71 than the coils 61, 81 with corresponding variation of pressure. The products from the coil 81 are passed under turbulent flow through a coil 10 in which the temperature is reduced, while being kept in the cracking range, into an insulated reaction drum 11. The vapours produced in the drum 11 are led through a pipe 12, a heat ecxhanger 4, a pipe 13 and a vaporizer 14 into contact with the raw material in heat exchanger 16 and the liquid fraction produced is transferred to the container 33 and retreated as previously described. The vapour fractions are led through a pipe 17 to a rectifier 18 down which is passed a spray of gasoline from a pipe 22 and part of the condensate is recirculated through a pipe 28 and a boiler 44. In the rectifier 18 the products are separated into a vapour fraction which is passed through a pipe 19, a heat exchanger 20, a pipe 24 and a cooler 25 to a storage tank 27, and a liquid fraction collected in a tank 35.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US277983TA | 1926-09-23 | 1926-09-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB277983A true GB277983A (en) | 1929-02-22 |
Family
ID=31945678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB25033/27A Expired GB277983A (en) | 1926-09-23 | 1927-09-22 |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB277983A (en) |
-
1927
- 1927-09-22 GB GB25033/27A patent/GB277983A/en not_active Expired
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