GB337380A - Improvements in cracking hydrocarbon oils - Google Patents
Improvements in cracking hydrocarbon oilsInfo
- Publication number
- GB337380A GB337380A GB2006029A GB2006029A GB337380A GB 337380 A GB337380 A GB 337380A GB 2006029 A GB2006029 A GB 2006029A GB 2006029 A GB2006029 A GB 2006029A GB 337380 A GB337380 A GB 337380A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tower
- vapours
- cracking
- zone
- condensate
- 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
-
- 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
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
337,380. Triggs, W. W., (Panhandle Refining Co.). June 29, 1929. Hydrocarbons, cracking.-In a process for ,cracking oils under reduced pressure, the oils are heated in a primary heating zone under suitable pressure at or above atmospheric and are then admitted to a flashing zone maintained under sub-atmospheric pressure, and the resulting vapours are passed to a cracking zone also under sub-atmospheric pressure. The crude oil is initially forced by a pump 54 through a preheating coil 57 into a flash pot 1 maintained at about 12-14 lbs. absolute pressure where the oil is vapourized and the vapours are passed through a cracking coil 56 at 1000-1200‹ and about 6-14 Ibs. pressure. The cracked vapours pass through a separating tower 6 and bubble towers 7, 8 where their temperature is controlled bv contact with cooling coils 26, 26<1>, 26<11>, 26<111>, 27, 28 through which the condensate from the towers 7, 8 is forced by pumps 13, 15 respectimely. Condensate from the tower 7 can also be injected into the tower 6 through a valve 18. The vapours from the tower 8 pass through a condenser 9 to a separator 10 from which condensate is withdrawn through a valve 29. The vacuum in the various parts of the system is determined by a pump 14 which withdraws vapours from the cracking zone through a line 40 and pumps them to the tower 6 through a line 39 or withdraws gases and uncondensed vapours 'from the separator 10 through a line 30 and pumps them through a line 42 to an absorption tower 11 supplied with washing liquid in the form of condensate withdrawn from the bottom of the tower 8. The condensate collecting at the bottom of the tower 11 is pumped by a pump 16 through a heat exchanger 17 and valve 33 into the middle of the tower 8. Burners 61 are provided in the upper portion of the furnace 2 as well as burners 62 in the lower zone, the burners' 61 being turned down after the plant is on flow, the coil 57 then being heated by waste gases of combustion passing through the perforations 63. In another construction the coils 56, 57 are arranged side by side and are separated by a wall. The burners 62 may be placed in arched side extensions of the zone 2 to avoid overheating the coil 56.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2006029A GB337380A (en) | 1929-06-29 | 1929-06-29 | Improvements in cracking hydrocarbon oils |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2006029A GB337380A (en) | 1929-06-29 | 1929-06-29 | Improvements in cracking hydrocarbon oils |
Publications (1)
Publication Number | Publication Date |
---|---|
GB337380A true GB337380A (en) | 1930-10-29 |
Family
ID=10139705
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2006029A Expired GB337380A (en) | 1929-06-29 | 1929-06-29 | Improvements in cracking hydrocarbon oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB337380A (en) |
-
1929
- 1929-06-29 GB GB2006029A patent/GB337380A/en not_active Expired
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