GB1529738A - Process for cracking crude oil - Google Patents
Process for cracking crude oilInfo
- Publication number
- GB1529738A GB1529738A GB449276A GB449276A GB1529738A GB 1529738 A GB1529738 A GB 1529738A GB 449276 A GB449276 A GB 449276A GB 449276 A GB449276 A GB 449276A GB 1529738 A GB1529738 A GB 1529738A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- crude oil
- gases
- passing
- mixing zone
- 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
- C10G9/34—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
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/20—C2-C4 olefins
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
1529738 Cracking crude oil UNION CARBIDE CORP 5 Feb 1976 [6 Feb 1975] 04492/76 Heading C5E Crude oil is cracked to provide lower olefins in a system comprising an atomization zone, a mixing zone, an adiabatic reaction zone and a quenching zone, at least the first three of these having a common axis by a process comprising:-(a) introducing into the mixing zone in a direction approximately perpendicular to said axis, a mixture of combustion gases produced from the essentially complete combustion of a fuel gas and oxygen mixed together with steam, at a subsonic velocity and an inlet temperature of 1000‹ C. to 2400‹ C. (b) introducing crude oil into the upstream end of the atomization zone in a downstream axial direction and in such a manner that crude oil is converted into droplets in the atomization zone; (c) passing the droplets of crude oil from the atomization zone into the gases in the mixing zone in a downstream axial direction in a ratio of 0À5 to 1 part by weight of crude oil per part by weight of gases and in such a manner that essentially all of the crude oil vaporizes into the gases in said mixing zone; (d) passing the effluent from the mixing zone into the reaction zone which has an outlet temperature of 600-1100‹ C., a pressure of 3-30 psig and the residence time is 6-60 milliseconds; (e) passing the effluent from (d) to a quenching zone which stops the reaction essentially instantaneously from which the product olefins are recovered. The system may also comprise a burner zone where the combustion gases are produced, the combustion gases being passed to the mixing zone through a restricted throat section which has the effect of accelerating the gases passing through.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US54746975A | 1975-02-06 | 1975-02-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1529738A true GB1529738A (en) | 1978-10-25 |
Family
ID=24184746
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB449276A Expired GB1529738A (en) | 1975-02-06 | 1976-02-05 | Process for cracking crude oil |
Country Status (8)
Country | Link |
---|---|
JP (1) | JPS51103106A (en) |
BE (1) | BE838290A (en) |
CA (1) | CA1047543A (en) |
DE (1) | DE2604392A1 (en) |
FR (1) | FR2333851A1 (en) |
GB (1) | GB1529738A (en) |
IT (1) | IT1054843B (en) |
NL (1) | NL7601183A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2469446A1 (en) * | 1979-11-13 | 1981-05-22 | Rockwell International Corp | PROCESS FOR THE RAPID PRODUCTION OF OLEFINS BY THERMAL CONVERSION OF HYDROCARBONS IN THE PRESENCE OF HYDROGEN |
EP0129501A1 (en) * | 1983-06-17 | 1984-12-27 | Mitsubishi Jukogyo Kabushiki Kaisha | Thermal cracking process for selectively producing olefins and aromatic hydrocarbons from hydrocarbons |
EP0143487A1 (en) * | 1983-10-31 | 1985-06-05 | Union Carbide Corporation | Control ACR product yields by adjustment of severity variables |
WO2022220996A1 (en) * | 2021-04-16 | 2022-10-20 | Exxonmobil Chemical Patents Inc. | Processes and systems for analyzing a sample separated from a steam cracker effluent |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2463800A1 (en) * | 1979-08-23 | 1981-02-27 | Algas Recources Ltd | Cracking hydrocarbon feeds to produce ethylene and synthesis gas - using gas filmed combustor, reactor and quench zone |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1186454A (en) * | 1956-11-10 | 1959-08-25 | Koppers Gmbh Heinrich | Process for the production of precious gaseous hydrocarbons |
FR1235328A (en) * | 1957-09-03 | 1960-07-08 | Huber Corp J M | Process and device for the production of carbon black |
CA1032561A (en) * | 1973-07-09 | 1978-06-06 | Gerard R. Kamm | Process for cracking crude oil |
-
1976
- 1976-01-06 CA CA242,995A patent/CA1047543A/en not_active Expired
- 1976-02-05 FR FR7603225A patent/FR2333851A1/en not_active Withdrawn
- 1976-02-05 IT IT1993976A patent/IT1054843B/en active
- 1976-02-05 GB GB449276A patent/GB1529738A/en not_active Expired
- 1976-02-05 BE BE164109A patent/BE838290A/en not_active IP Right Cessation
- 1976-02-05 JP JP1089476A patent/JPS51103106A/en active Pending
- 1976-02-05 NL NL7601183A patent/NL7601183A/en not_active Application Discontinuation
- 1976-02-05 DE DE19762604392 patent/DE2604392A1/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2469446A1 (en) * | 1979-11-13 | 1981-05-22 | Rockwell International Corp | PROCESS FOR THE RAPID PRODUCTION OF OLEFINS BY THERMAL CONVERSION OF HYDROCARBONS IN THE PRESENCE OF HYDROGEN |
EP0129501A1 (en) * | 1983-06-17 | 1984-12-27 | Mitsubishi Jukogyo Kabushiki Kaisha | Thermal cracking process for selectively producing olefins and aromatic hydrocarbons from hydrocarbons |
EP0143487A1 (en) * | 1983-10-31 | 1985-06-05 | Union Carbide Corporation | Control ACR product yields by adjustment of severity variables |
WO2022220996A1 (en) * | 2021-04-16 | 2022-10-20 | Exxonmobil Chemical Patents Inc. | Processes and systems for analyzing a sample separated from a steam cracker effluent |
Also Published As
Publication number | Publication date |
---|---|
BE838290A (en) | 1976-08-05 |
IT1054843B (en) | 1981-11-30 |
JPS51103106A (en) | 1976-09-11 |
CA1047543A (en) | 1979-01-30 |
FR2333851A1 (en) | 1977-07-01 |
NL7601183A (en) | 1976-08-10 |
DE2604392A1 (en) | 1976-08-19 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |