GB560195A - Improvements in or relating to the production of olefines by the treatment of hydrocarbon oils at elevated temperatures - Google Patents
Improvements in or relating to the production of olefines by the treatment of hydrocarbon oils at elevated temperaturesInfo
- Publication number
- GB560195A GB560195A GB8289/42A GB828942A GB560195A GB 560195 A GB560195 A GB 560195A GB 8289/42 A GB8289/42 A GB 8289/42A GB 828942 A GB828942 A GB 828942A GB 560195 A GB560195 A GB 560195A
- Authority
- GB
- United Kingdom
- Prior art keywords
- line
- tower
- oil
- gases
- vapors
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
-
- 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
- C10G9/34—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts
- C10G9/36—Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils by direct contact with inert preheated fluids, e.g. with molten metals or salts with heated gases or vapours
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (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 Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0560195/IV/1> <PICT:0560195/IV/2> Heavy hydrocarbon oils are converted mainly into gaseous unsaturated hydrocarbons, e.g. ethylene, propylene, butadiene, and aromatic hydrocarbons, e.g. toluene, benzene and xylene by vaporising the oil in presence of super-heated steam, separating unvaporised constituents, and passing the vapors and gases through a conversion zone heated to 1200-1300 DEG F., quenching the converted products with a condensate produced later in the process, fractionating the vapors to separate gasoline and gases from a condensate which is used as the quenching oil and further fractionating the gasoline and gases to recover ethylene. Crude oil, e.g. gas oil, is fed through line 10 and preheater 14 into a vaporising coil 18 in a furnace 22 and is mixed with superheated steam in the latter sections of the coil. The mixed vapors and liquid pass to a separating tower 42 where liquids are separated through line 44. Superheated steam may be added at the base of the tower through line 102. The vapors pass overhead through line 48 to the conversion coil 55 and the cracked products are quenched in line 56 and then pass to a combined separator and fractionator 60, 62 where a condensate is collected on a tray 72 and recycled through line 74, 78 as quenching oil. This oil is preferably cooled by passing it through cooler 14 where it preheats the charge and through cooler 32 where it preheats water passing to the superheating coil 37. The condensate may also be cycled (a) through line 47 as reflux to tower 42 (b) through line 68 to the separator 60 (c) through line 96 to tower 62. Vapors and gases passing overhead from tower 62 are collected in separator 112 and subjected to a series of compressions and separations in receivers 126, 142, 154 and compressors 136, 150 to obtain a liquid fraction which is fractionated in tower 174 to recover as bottoms an aromatic gasoline fraction recovered through lines 178, 184 and an over-head which is mixed with gases from receiver 154 compressed in compressor 201 and fractionated in tower 202 to separate ethylene and like gaseous fractions. A combination type furnace for carrying out the various heating operations required comprises (Fig. 2) radiant and convection heating sections 232, 234 heated by roof burners 236, and end burners 240. The oil is first heated in a preheating section 246, and is then divided into two, steam passing through tube banks 242, 244 and uniting in line 264. Steam is superheated and fed through line 252, 260 into the banks at 258, 262.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US560195XA | 1941-01-02 | 1941-01-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB560195A true GB560195A (en) | 1944-03-24 |
Family
ID=22001640
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8289/42A Expired GB560195A (en) | 1941-01-02 | 1942-06-17 | Improvements in or relating to the production of olefines by the treatment of hydrocarbon oils at elevated temperatures |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB560195A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0074435A2 (en) * | 1981-09-08 | 1983-03-23 | Dow Chemical (Nederland) B.V. | Process and apparatus for cracking hydrocarbon; mixing device; apparatus and process for producing superheated steam; radiation block structure |
EP2382040A2 (en) * | 2009-01-26 | 2011-11-02 | Lummus Technology Inc. | Adiabatic reactor to produce olefins |
-
1942
- 1942-06-17 GB GB8289/42A patent/GB560195A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0074435A2 (en) * | 1981-09-08 | 1983-03-23 | Dow Chemical (Nederland) B.V. | Process and apparatus for cracking hydrocarbon; mixing device; apparatus and process for producing superheated steam; radiation block structure |
EP0074435A3 (en) * | 1981-09-08 | 1983-05-04 | Dow Chemical (Nederland) B.V. | Process and apparatus for cracking hydrocarbon; mixing device; apparatus and process for producing superheated steam; radiation block structure |
EP2382040A2 (en) * | 2009-01-26 | 2011-11-02 | Lummus Technology Inc. | Adiabatic reactor to produce olefins |
EP2382040A4 (en) * | 2009-01-26 | 2014-05-14 | Lummus Technology Inc | Adiabatic reactor to produce olefins |
US8815080B2 (en) | 2009-01-26 | 2014-08-26 | Lummus Technology Inc. | Adiabatic reactor to produce olefins |
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