GB831105A - Improvements in the production of acetylene by thermal cracking of hydrocarbons - Google Patents
Improvements in the production of acetylene by thermal cracking of hydrocarbonsInfo
- Publication number
- GB831105A GB831105A GB23074/58A GB2307458A GB831105A GB 831105 A GB831105 A GB 831105A GB 23074/58 A GB23074/58 A GB 23074/58A GB 2307458 A GB2307458 A GB 2307458A GB 831105 A GB831105 A GB 831105A
- Authority
- GB
- United Kingdom
- Prior art keywords
- water
- gas stream
- acetylene
- pressure
- preheater
- 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
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/76—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
- C07C2/78—Processes with partial combustion
-
- 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
-
- 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
- C10G9/38—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 produced by partial combustion of the material to be cracked or by combustion of another hydrocarbon
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A process for the production of acetylene by partial oxidation of gaseous or vaporized hydrocarbons and rapid cooling of the reaction gas by the introduction of water into the gas stream comprises introducing water into the gas stream in the form of undivided jets and so selecting conditions that for a gas stream with a dynamic pressure (PD) and a depth of penetration (a) of water into the gas stream, a diameter (d) of the jets and the water pressure (PW) immediately at the outlet openings of the water nozzles, the numerical values of the expression PW/PD x d/a lie between 1 and 15 In a typical example, 20,000 normal metres per hour of methane are heated to 540 DEG C. in a preheater and 1150 normal cubic metres per hour of oxygen are heated to 540 DEG C. in a second preheater. After thorough mixing the gases enter through parallel channels into a reaction chamber in which the methane reacts with the oxygen with the formation of a flame. The diameter of the reaction gas at the outlet is 40 mms. and the pressure (PD) is 2.2 X 10-3 atmospheres. The reaction gas is rapidly cooled and a mixture obtained which contains 7.82% by volume of acetylene and 4.28 grams per cu. metre of carbon black.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE831105X | 1957-08-03 | ||
DE1200694X | 1957-08-03 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB831105A true GB831105A (en) | 1960-03-23 |
Family
ID=25949538
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB23074/58A Expired GB831105A (en) | 1957-08-03 | 1958-07-18 | Improvements in the production of acetylene by thermal cracking of hydrocarbons |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR1200694A (en) |
GB (1) | GB831105A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3396207A (en) * | 1957-08-03 | 1968-08-06 | Basf Ag | Production of acetylene by thermal cracking of hydrocarbons |
-
1958
- 1958-07-18 GB GB23074/58A patent/GB831105A/en not_active Expired
- 1958-07-29 FR FR1200694D patent/FR1200694A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3396207A (en) * | 1957-08-03 | 1968-08-06 | Basf Ag | Production of acetylene by thermal cracking of hydrocarbons |
Also Published As
Publication number | Publication date |
---|---|
FR1200694A (en) | 1959-12-23 |
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