GB264845A - Improvements in and relating to the conversion of saturated hydrocarbons, in gas or vapour form, especially methane, into unsaturated hydrocarbons - Google Patents
Improvements in and relating to the conversion of saturated hydrocarbons, in gas or vapour form, especially methane, into unsaturated hydrocarbonsInfo
- Publication number
- GB264845A GB264845A GB1627/27A GB162727A GB264845A GB 264845 A GB264845 A GB 264845A GB 1627/27 A GB1627/27 A GB 1627/27A GB 162727 A GB162727 A GB 162727A GB 264845 A GB264845 A GB 264845A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- burners
- tube
- hydrocarbons
- nozzles
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Catalysts (AREA)
Abstract
264,845. I. G. Farbenindustric Akt.- Ges. Jan. 20, 1926, [Convention date]. Hydrocarbons; benzene; acetaldehyde. - The thermal decomposition of gaseous or vaporous saturated hydrocarbons, particularly methane, into unsaturated hydrocarbons, particularly acetylene. is effected by passing the saturated hydrocarbons, alone or diluted with nitrogen or other inert gases, through a flame which extends across substantially the whole cross-sectional area of a tube. The flame may be a disc-like flame produced by burning a combustible gas, such as a part of the gas to be treated, with air &c. in a plurality of separate burners. The reaction products may be rapidly cooled to separate the hydrocarbons, or they may be subjected directly to further chemical treatment to vield other products, such as benzene or acetaldehyde. The residual gases containing hydrogen and carbon monoxide may be converted catalytically into methane, which may be returned to the process. Suitable apparatus comprises an inlet tube E for the gas to be treated having branches m and a main branch R controlled by taps F, g. The branches m lead to burners i arranged radially in a horizontal plane, as shown in Fig. 2, and projecting into a reaction tube K; the burners have flattened nozzles and are fed with air &c. through pipes h. In use, the burners are lit by an ignition device (not shown), such as an induction sparking apparatus, and the main part of the gas to be treated flows through the tube R and then through the disc of flame produced by the burners. The reaction products preheat the gases flowing in the tube R and are withdrawn through a pipe S. The air &c. and/or the combustion gas may be preheated, preferably by exchange of heat with the reaction products. The Specification as open to inspection under Sect. 91 (3) (a) states that the thermal decomposition may be effected in a zone of high temperature obtained by the flameless combustion of part of the gas to be treated. In this connection a modified apparatus is described in which the burners i are replaced by 32 radially disposed oxygen-delivering nozzles and in which the reaction tube is fitted internally, at the level of the nozzles, with a horizontally arranged gauze of tungsten wire covering the whole cross-section of the tube and supporting a thin layer of platinized asbestos. A further modification is described also in which the platinized asbestos is replaced by a plate of highly porous refractory material, such as " Marquardt composition," mounted about 1 cm. below the nozzles. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE264845X | 1926-01-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB264845A true GB264845A (en) | 1928-05-21 |
Family
ID=5991442
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1627/27A Expired GB264845A (en) | 1926-01-20 | 1927-01-19 | Improvements in and relating to the conversion of saturated hydrocarbons, in gas or vapour form, especially methane, into unsaturated hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB264845A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2223988A1 (en) * | 2009-02-17 | 2010-09-01 | ISP Marl GmbH | Purification of an aromatic fraction containing acetylenes by selective hydrogenation of the acetylenes |
-
1927
- 1927-01-19 GB GB1627/27A patent/GB264845A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2223988A1 (en) * | 2009-02-17 | 2010-09-01 | ISP Marl GmbH | Purification of an aromatic fraction containing acetylenes by selective hydrogenation of the acetylenes |
EP2223987A1 (en) * | 2009-02-17 | 2010-09-01 | ISP Marl GmbH | Purification of an aromatic fraction containing acetylenes by selective hydrogenation of the acetylenes |
US8293959B2 (en) | 2009-02-17 | 2012-10-23 | Isp Investment Inc. | Purification of an aromatic fraction containing acetylenes by selective hydrogenation of the acetylenes |
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