GB701100A - Improvements in and relating to oil cracking and volatilization apparatus - Google Patents
Improvements in and relating to oil cracking and volatilization apparatusInfo
- Publication number
- GB701100A GB701100A GB1466850A GB1466850A GB701100A GB 701100 A GB701100 A GB 701100A GB 1466850 A GB1466850 A GB 1466850A GB 1466850 A GB1466850 A GB 1466850A GB 701100 A GB701100 A GB 701100A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- oil
- heating elements
- heaters
- vertical shafts
- 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
- C10G15/00—Cracking of hydrocarbon oils by electric means, electromagnetic or mechanical vibrations, by particle radiation or with gases superheated in electric arcs
-
- 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
- C10G9/06—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by pressure distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Thermal Sciences (AREA)
- Electromagnetism (AREA)
- Mechanical Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
<PICT:0701100/III/1> <PICT:0701100/III/2> An apparatus for cracking oils comprises a chamber containing a source of electrical discharge such as arc discharge electrodes, means to circulate the oil in the chamber, and electric immersion heaters or other heating means for heating the oil prior to electrification. Fig. 1 is a side view and Fig. 2 an end view of a rectangular tank 1 which contains six rows of rod-like electric heating elements 3, disposed in pairs, at three different heights. Secured through the side walls of the chamber, intermediate the pairs of heating elements 3, are arc discharge electrodes 6. Three vertical shafts 12 are mounted in the chamber. The upper ends of these vertical shafts carry bevel wheels 11 which mesh with bevel wheels 10 journalled on horizontal shaft 8. The lower ends of vertical shafts 12 have conical oil throwers 14 mounted thereon, the outer surfaces of these throwers being provided with a series of oppositely opposed oil cups 15. Oil is fed into the chamber through inlet 2. Power is supplied to heating elements 3 until the oil has been raised to 120 DEG -130 DEG F. An electric motor (not shown), preferably reversible, connected to pulley 9, is switched on, thus causing shafts 12 to rotate whereby cups 15 circulate the oil. Power is supplied to electrodes 6. The vapours formed by the cracking, pass out of the chamber through outlets 16. Three float switches 19, each of which controls the supply of current to two corresponding rows of heaters 3, are mounted on the side walls of the chamber; the arrangement being such that as the level of oil in the chamber descends, so the float switch above the level of oil will cut out its associated heaters. The temperature of the chamber is not allowed to rise above 400 DEG F. The inner surface of the chamber is preferably lined with porcelain.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1466850A GB701100A (en) | 1950-06-12 | 1950-06-12 | Improvements in and relating to oil cracking and volatilization apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1466850A GB701100A (en) | 1950-06-12 | 1950-06-12 | Improvements in and relating to oil cracking and volatilization apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
GB701100A true GB701100A (en) | 1953-12-16 |
Family
ID=10045427
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1466850A Expired GB701100A (en) | 1950-06-12 | 1950-06-12 | Improvements in and relating to oil cracking and volatilization apparatus |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB701100A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009072932A2 (en) * | 2007-12-05 | 2009-06-11 | Vladimir Schukin | Method for steam cracking of oil refined products |
-
1950
- 1950-06-12 GB GB1466850A patent/GB701100A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009072932A2 (en) * | 2007-12-05 | 2009-06-11 | Vladimir Schukin | Method for steam cracking of oil refined products |
WO2009072932A3 (en) * | 2007-12-05 | 2009-10-22 | Schukin Vladimir | Method for steam cracking of oil refined products |
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