GB1077918A - Process for the production of ethylene - Google Patents
Process for the production of ethyleneInfo
- Publication number
- GB1077918A GB1077918A GB4682265A GB4682265A GB1077918A GB 1077918 A GB1077918 A GB 1077918A GB 4682265 A GB4682265 A GB 4682265A GB 4682265 A GB4682265 A GB 4682265A GB 1077918 A GB1077918 A GB 1077918A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ethylene
- pyrolysis
- propane
- steam
- tube
- 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
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 title abstract 2
- 239000005977 Ethylene Substances 0.000 title abstract 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 abstract 4
- 238000000197 pyrolysis Methods 0.000 abstract 3
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 abstract 2
- 239000001294 propane Substances 0.000 abstract 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract 1
- 239000005864 Sulphur Substances 0.000 abstract 1
- 239000000571 coke Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 abstract 1
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
- C10G9/16—Preventing or removing incrustation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
- C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
- C07C4/04—Thermal processes
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Ethylene and/or propylene are obtained by pyrolysis of a gas containing ethane and/or propane by mixing with steam and pyrolysing in an indirectly heated pyrolysis zone to convert at least 50% of the ethane and at least 85% of the propane, withdrawing at a temperature of at least 1500 DEG F. after not more than 1 second and cooling to below 1000 DEG F. Preferably there is added to the feed 50-1000 p.p.m. of sulphur and pyrolysis is effected in a tube of 3-6 inches outside diameter to which is applied 20,000-40,000 B.T.L.U./hr./sq. ft. Coke may be removed periodically by passing only steam through the tube at at least 1800 DEG F.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US40914964A | 1964-11-05 | 1964-11-05 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1077918A true GB1077918A (en) | 1967-08-02 |
Family
ID=23619245
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB4682265A Expired GB1077918A (en) | 1964-11-05 | 1965-11-04 | Process for the production of ethylene |
Country Status (5)
| Country | Link |
|---|---|
| BE (1) | BE671949A (en) |
| DE (1) | DE1543156A1 (en) |
| ES (1) | ES319054A1 (en) |
| GB (1) | GB1077918A (en) |
| NL (1) | NL6514389A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4379046A (en) | 1981-06-11 | 1983-04-05 | Exxon Research & Engineering Co. | Integrated two stage coking and steam cracking process and apparatus therefor |
| US4411769A (en) | 1982-03-23 | 1983-10-25 | Exxon Research & Engineering Co. | Integrated two stage coking and steam cracking process and apparatus therefor |
| US4436540A (en) | 1982-10-15 | 1984-03-13 | Exxon Research & Engineering Co. | Low pressure separation for light hydrocarbon recovery |
| US4457364A (en) * | 1982-03-18 | 1984-07-03 | Exxon Research & Engineering Co. | Close-coupled transfer line heat exchanger unit |
| US4614229A (en) * | 1983-06-20 | 1986-09-30 | Exxon Research & Engineering Co. | Method and apparatus for efficient recovery of heat from hot gases that tend to foul heat exchanger tubes |
| EP0905110A3 (en) * | 1997-09-24 | 1999-10-06 | BP Chemicals Limited | Hydrocarbon cracking process |
| CN104781217A (en) * | 2012-09-20 | 2015-07-15 | 林德股份公司 | Plant and process for preparing ethylene |
-
1965
- 1965-10-28 DE DE19651543156 patent/DE1543156A1/en active Pending
- 1965-10-29 ES ES0319054A patent/ES319054A1/en not_active Expired
- 1965-11-04 GB GB4682265A patent/GB1077918A/en not_active Expired
- 1965-11-05 NL NL6514389A patent/NL6514389A/xx unknown
- 1965-11-05 BE BE671949D patent/BE671949A/xx unknown
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4379046A (en) | 1981-06-11 | 1983-04-05 | Exxon Research & Engineering Co. | Integrated two stage coking and steam cracking process and apparatus therefor |
| US4457364A (en) * | 1982-03-18 | 1984-07-03 | Exxon Research & Engineering Co. | Close-coupled transfer line heat exchanger unit |
| US4411769A (en) | 1982-03-23 | 1983-10-25 | Exxon Research & Engineering Co. | Integrated two stage coking and steam cracking process and apparatus therefor |
| US4436540A (en) | 1982-10-15 | 1984-03-13 | Exxon Research & Engineering Co. | Low pressure separation for light hydrocarbon recovery |
| US4614229A (en) * | 1983-06-20 | 1986-09-30 | Exxon Research & Engineering Co. | Method and apparatus for efficient recovery of heat from hot gases that tend to foul heat exchanger tubes |
| EP0905110A3 (en) * | 1997-09-24 | 1999-10-06 | BP Chemicals Limited | Hydrocarbon cracking process |
| CN104781217A (en) * | 2012-09-20 | 2015-07-15 | 林德股份公司 | Plant and process for preparing ethylene |
| JP2015529230A (en) * | 2012-09-20 | 2015-10-05 | リンデ アクチエンゲゼルシャフトLinde Aktiengesellschaft | Equipment and method for producing ethylene |
| CN104781217B (en) * | 2012-09-20 | 2016-11-09 | 林德股份公司 | Apparatus and method for producing ethylene |
Also Published As
| Publication number | Publication date |
|---|---|
| DE1543156A1 (en) | 1969-07-31 |
| NL6514389A (en) | 1966-05-06 |
| BE671949A (en) | 1966-03-01 |
| ES319054A1 (en) | 1966-05-01 |
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