GB978181A - Process for the dehydrogenation of hydrocarbons - Google Patents
Process for the dehydrogenation of hydrocarbonsInfo
- Publication number
- GB978181A GB978181A GB1838263A GB1838263A GB978181A GB 978181 A GB978181 A GB 978181A GB 1838263 A GB1838263 A GB 1838263A GB 1838263 A GB1838263 A GB 1838263A GB 978181 A GB978181 A GB 978181A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acceptor
- halogen
- reaction
- solid
- added
- 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
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/42—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor
- C07C5/44—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with halogen or a halogen-containing compound as an acceptor
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0978181/C4-C5/1> <PICT:0978181/C4-C5/2> Hydrocarbons are dehydrogenated by reaction with iodine or bromine by passing the reactants through an elongated chamber having a length to diameter ratio of at least 10 together with a solid acceptor capable of binding hydrogen halide as inorganic halide. The acceptor used is preferably one which can be regenerated after use back into acceptor and halogen by reaction with oxygen as described in Specification 895,500, and may be supported on a carrier. In one embodiment the regeneration and reaction are effected simultaneously and continuously in two elongated tubes joined end to end or one outside the other coaxially or in a single tube. Reactants and solid may flow upwards or downwards. In Fig. 1 a fluidized bed of solid 4 is entrained by an oxygen-containing gas and flows upwardly through regeneration tube 1. Hydrocarbons are introduced by line 3 and react with regenerated halogen in the outer reactor tube and products recovered by line 7. In order to avoid loss of halogen a nitrogenous base, preferably ammonia, is added to the reaction effluent and then the effluent is cooled to 85-150 DEG C. The base is preferably added as an aqueous solution together with an organic solvent to prevent formation of tar. The halogen is recovered by decomposing the product by contact with the solid acceptor in the regenerator or a separate chamber. In Fig. 2, acceptor is regenerated in the lower half of tube 1 with oxygen from inlet 2 and hydrocarbon is added at 3. Nitrogenous base is added by line 8 in separator 5 together with recovered base from chamber 17. After further cyclone separator 7 the effluent is cooled and the condensate passed from separator 12 by line 16 to contact acceptor material in chamber 17 where the halogen is bound by the acceptor.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL278333 | 1962-05-11 | ||
NL289388 | 1963-02-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB978181A true GB978181A (en) | 1964-12-16 |
Family
ID=26641834
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1838263A Expired GB978181A (en) | 1962-05-11 | 1963-05-09 | Process for the dehydrogenation of hydrocarbons |
Country Status (2)
Country | Link |
---|---|
ES (1) | ES287853A1 (en) |
GB (1) | GB978181A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999067193A1 (en) * | 1998-06-24 | 1999-12-29 | Kozaczko Jozef | Method for producing hydrocarbons |
CN104907001A (en) * | 2015-06-18 | 2015-09-16 | 中冶焦耐工程技术有限公司 | High-pressure separator for benzene hydrogenation device and use method of high-pressure separator for benzene hydrogenation device |
-
1963
- 1963-05-09 GB GB1838263A patent/GB978181A/en not_active Expired
- 1963-05-09 ES ES287853A patent/ES287853A1/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999067193A1 (en) * | 1998-06-24 | 1999-12-29 | Kozaczko Jozef | Method for producing hydrocarbons |
CN104907001A (en) * | 2015-06-18 | 2015-09-16 | 中冶焦耐工程技术有限公司 | High-pressure separator for benzene hydrogenation device and use method of high-pressure separator for benzene hydrogenation device |
CN104907001B (en) * | 2015-06-18 | 2017-07-28 | 中冶焦耐工程技术有限公司 | A kind of high-pressure separator and application method for benzol hydro refining unit |
Also Published As
Publication number | Publication date |
---|---|
ES287853A1 (en) | 1963-08-01 |
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