GB593989A - Improvements in or relating to vapor phase isomerization processes - Google Patents
Improvements in or relating to vapor phase isomerization processesInfo
- Publication number
- GB593989A GB593989A GB15907/45A GB1590745A GB593989A GB 593989 A GB593989 A GB 593989A GB 15907/45 A GB15907/45 A GB 15907/45A GB 1590745 A GB1590745 A GB 1590745A GB 593989 A GB593989 A GB 593989A
- Authority
- GB
- United Kingdom
- Prior art keywords
- bed
- line
- isomerization
- paraffin
- vessel
- 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
- 238000006317 isomerization reaction Methods 0.000 title abstract 9
- 238000000034 method Methods 0.000 title 1
- VSCWAEJMTAWNJL-UHFFFAOYSA-K Aluminium chloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 abstract 12
- 239000012188 paraffin wax Substances 0.000 abstract 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract 6
- 239000003054 catalyst Substances 0.000 abstract 6
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 abstract 6
- 229910000041 hydrogen chloride Inorganic materials 0.000 abstract 6
- 229910001507 metal halide Inorganic materials 0.000 abstract 6
- 150000005309 metal halides Chemical class 0.000 abstract 6
- 229910000039 hydrogen halide Inorganic materials 0.000 abstract 4
- 239000012433 hydrogen halide Substances 0.000 abstract 4
- 239000002250 absorbent Substances 0.000 abstract 3
- 230000002745 absorbent Effects 0.000 abstract 3
- 239000003463 adsorbent Substances 0.000 abstract 3
- 239000004215 Carbon black (E152) Substances 0.000 abstract 2
- 229910001570 bauxite Inorganic materials 0.000 abstract 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 abstract 2
- 150000004820 halides Chemical class 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- 230000008929 regeneration Effects 0.000 abstract 2
- 238000011069 regeneration method Methods 0.000 abstract 2
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
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2702—Catalytic processes not covered by C07C5/2732 - C07C5/31; Catalytic processes covered by both C07C5/2732 and C07C5/277 simultaneously
- C07C5/271—Catalytic processes not covered by C07C5/2732 - C07C5/31; Catalytic processes covered by both C07C5/2732 and C07C5/277 simultaneously with inorganic acids; with salts or anhydrides of acids
- C07C5/2718—Acids of halogen; Salts thereof; complexes thereof with organic compounds
- C07C5/2721—Metal halides; Complexes thereof with organic compounds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
In the isomerization of paraffins by passage in the presence of hydrogen halide over a heated catalyst bed comprising a metal halide absorbed on a porous support, metal halide vapours are added to one portion of the catalyst bed to reactivate it while the supply of hydrogen halide thereto is discontinued, while isomerization is continued in another portion of the bed wherein the metal halide vapours are in equilibrium with the halide absorbed on the support. A paraffin such as n-butane is heated and fed by line 15 to a vessel 16 containing aluminium chloride which is sublimed and carried by the stream via line 18 to reactor 19 where it is deposited on an absorbent 20 such as bauxite or "Porocel" (Registered Trade Mark). When the absorbent becomes saturated, vessel 16 is bye-passed and hydrogen chloride introduced into line 18 by line 25 and valve 24, isomerization of the paraffin then proceeding. When the bed 20 requires regeneration, the paraffin feed is passed through vessel 16 again, and valve 24 is closed to withhold hydrogen chloride from the lower part of bed 20. Valve 27 is at the same time opened to supply <PICT:0593989/III/1> hydrogen chloride to the upper part of the bed through pipe 29 and jets 30. The temperature of the paraffin feed may be increased to compensate for the smaller volume of catalyst bed used in isomerization. The amount of aluminium chloride added during reactivation should not exceed 5 per cent. by weight of the total absorbent to avoid fouling of the upper part of the bed. In an example, temperature is raised from 270-300 DEG F. during a 10 day operation, with 4-7 per cent. addition of promoter based on the weight of hydrocarbon. Reactivation is effected by adding 2-3 per cent. of aluminium chloride by line 18 while the upper part of the bed is isomerizing at about 290-300 DEG F. The different sections of the bed may consist of a number of separate vessels in series.ALSO:<PICT:0593989/IV/1> In the isomerization of paraffins by passage in the presence of hydrogen halide over a heated catalyst bed comprising a metal halide adsorbed on a porous support, metal halide vapours are added to one portion of the catalyst bed to reactivate it while the supply of hydrogen halide thereto is discontinued, while isomerization is continued in another portion of the bed wherein the metal halide vapours are in equilibrium with the halide adsorbed on the support. A paraffin such as n-butane is heated and fed by line 15 to a vessel 16 containing aluminium chloride which is sublimed and carried by the stream via line 18 to reactor 19 where it is deposited on an adsorbent 20 such as bauxite or "Porocel" (Registered Trade Mark). When the adsorbent becomes saturated, vessel 16 is byepassed and hydrogen chloride introduced into line 18 by line 25 and valve 24, isomerization of the paraffin then proceeding. When the bed 20 requires regeneration, the paraffin feed is passed through vessel 16 again, and valve 24 is closed to withhold hydrogen chloride from the lower part of bed 20. Valve 27 is at the same time opened to supply hydrogen chloride to the upper part of the base through pipe 29 and jets 30. The temperature of the paraffin feed may be increased to compensate for the smaller volume of catalyst bed used in isomerization. The amount of aluminium chloride added during reactivation should not exceed 5 per cent by weight of the total adsorbent to avoid fouling of the upper part of the bed. In an example, temperature is raised from 270-300 DEG F. during a 10-day operation, with 4-7 per cent addition of promoter based on the weight of hydrocarbon. Reactivation is effected by adding 2-3 per cent of aluminium chloride by line 18 while the upper part of the bed is isomerizing at about 290-300 DEG F. The different sections of the bed may consist of a number of separate vessels in series.
Publications (1)
Publication Number | Publication Date |
---|---|
GB593989A true GB593989A (en) | 1947-10-30 |
Family
ID=1731907
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB15907/45A Expired GB593989A (en) | 1945-06-21 | Improvements in or relating to vapor phase isomerization processes |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB593989A (en) |
-
1945
- 1945-06-21 GB GB15907/45A patent/GB593989A/en not_active Expired
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