GB253489A - Improvements in or relating to the distillation of liquids such as petroleum and similar hydrocarbons - Google Patents
Improvements in or relating to the distillation of liquids such as petroleum and similar hydrocarbonsInfo
- Publication number
- GB253489A GB253489A GB10444/26A GB1044426A GB253489A GB 253489 A GB253489 A GB 253489A GB 10444/26 A GB10444/26 A GB 10444/26A GB 1044426 A GB1044426 A GB 1044426A GB 253489 A GB253489 A GB 253489A
- Authority
- GB
- United Kingdom
- Prior art keywords
- passed
- pipe
- chambers
- pump
- residue
- 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
- C10G7/00—Distillation of hydrocarbon oils
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
253,489. Bataafsche Petroleum Maatschappij. June 13, 1925, [Convention date]. Separate heater and evaporator apparatus.-In distilling hydrocarbon oils by the method of heat. ing the oil by passage through a tube furnace, and discharging the heated oil into vapour-separating chambers, the chambers and the subsequent dephlegmators and condensers are maintained under high vacuum. Oil from a container 1 is passed by a pump 2 through a tube furnace 4, and discharged into a vaporizing chamber 5 in which the liquid runs down the walls, and to which steam is passed by a pipe 6. Vapours pass through a rectifier 14, a dephlegmator 19, and condenser 21 leading to a condensate tank 22 evacuated by a vacuum pump. Unvaporized residue is withdrawn through a cooler 8 to a container 9 connected by a pipe 10 to a vacuum pump, or the hot residue is forced bv a pump through a second pipe coil in the furnace and into a second vaporizing chamber, the residue from which is passed through a third coil. The vapours from the second and third vaporizing chambers are treated in separate rectifiers, dephlegmators and condensers.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL253489X | 1925-06-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB253489A true GB253489A (en) | 1927-02-03 |
Family
ID=19781201
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10444/26A Expired GB253489A (en) | 1925-06-13 | 1926-04-20 | Improvements in or relating to the distillation of liquids such as petroleum and similar hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB253489A (en) |
-
1926
- 1926-04-20 GB GB10444/26A patent/GB253489A/en not_active Expired
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